U.S. patent number 7,026,420 [Application Number 10/987,832] was granted by the patent office on 2006-04-11 for aqueous room temperature living radical polymerization of vinyl halides.
This patent grant is currently assigned to University of Pennsylvania. Invention is credited to Virgil Percec, Anatoliy V. Popov.
United States Patent |
7,026,420 |
Percec , et al. |
April 11, 2006 |
**Please see images for:
( Certificate of Correction ) ** |
Aqueous room temperature living radical polymerization of vinyl
halides
Abstract
A living polymerization process for preparation of poly(vinyl
chloride) (PVC) with controlled molecular weight and molecular
weight distribution is described. The polymerization reaction can
be initiated by various polyhalocarbon initiators in conjunction
with non-metallic reducing single electron transfer reagents as
catalysts and accelerated by electron shuttles. The process occurs
at room temperature in water or water-organic solvent medium. The
polymerization provides PVC with a controlled molecular weight and
narrow molecular weight distribution. The halogen containing
polymer compositions are useful as, among others, viscosity
modifiers, impact modifiers and compatibilizers.
Inventors: |
Percec; Virgil (Philadelphia,
PA), Popov; Anatoliy V. (Philadelphia, PA) |
Assignee: |
University of Pennsylvania
(Philadelphia, PA)
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Family
ID: |
34657830 |
Appl.
No.: |
10/987,832 |
Filed: |
November 12, 2004 |
Prior Publication Data
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Document
Identifier |
Publication Date |
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US 20050148734 A1 |
Jul 7, 2005 |
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Related U.S. Patent Documents
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Application
Number |
Filing Date |
Patent Number |
Issue Date |
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10179584 |
Jun 24, 2002 |
6911515 |
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09893201 |
Jun 27, 2001 |
6838535 |
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60278114 |
Mar 23, 2001 |
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Current U.S.
Class: |
526/344 |
Current CPC
Class: |
C08F
14/06 (20130101); C08F 2/10 (20130101); C08F
14/02 (20130101); C08F 2/38 (20130101); C08F
14/02 (20130101); C08F 2/10 (20130101) |
Current International
Class: |
C08F
14/06 (20060101) |
Field of
Search: |
;526/344 |
References Cited
[Referenced By]
U.S. Patent Documents
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2831844 |
April 1958 |
Simpson et al. |
2996470 |
August 1961 |
Cole et al. |
4091197 |
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Fischer et al. |
4511700 |
April 1985 |
Melby et al. |
5455319 |
October 1995 |
Bak et al. |
5763548 |
June 1998 |
Matyjaszewski et al. |
5789487 |
August 1998 |
Matyjaszewski et al. |
5807937 |
September 1998 |
Matyjaszewski et al. |
6162882 |
December 2000 |
Matyjaszewski et al. |
6838535 |
January 2005 |
Percec et al. |
6911515 |
June 2005 |
Percec et al. |
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WO 96/30421 |
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May 1997 |
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WO |
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Primary Examiner: Harlan; Robert D.
Attorney, Agent or Firm: Hudak, Shunk & Farine Co.
LPA
Parent Case Text
CROSS REFERENCE
This is a division of application Ser. No. 10/179,584, filed on
Jun. 24, 2002 now U.S. Pat. No. 6,911,515, which is a
continuation-in-part of related application Ser. No. 09/893,201
filed Jun. 27, 2001 now U.S. Pat. No. 6,838,535, which claims the
benefit of U.S. Provisional Application 60/278,114 filed Mar. 23,
2001.
Claims
What is claimed is:
1. A process for the preparation of a chlorine containing polymer
comprising the steps of: forming a mixture comprising a vinyl
chloride monomer; and optionally, a comonomer, in the presence of:
an initiator, a metal-free catalyst; and optionally, a buffer, an
electron shuttle, a surfactant; and a solvent or water; and
polymerizing said vinyl chloride monomer to form a polymer or
copolymer by or a living radical process.
2. A process according to claim 1, wherein said initiator is a
halogen containing initiator.
3. A process according to claim 2, wherein said initiator is a
halogen containing initiator and said initiator contains one or
more of a mono, di, tri or polyfunctional
.alpha.,.alpha.-dihaloalkane,
.alpha.,.alpha.,.alpha.-trihaloalkane, a perhaloalkane, a
perfloroalkyl halide, a benzyl halide, an allyl halide, a sulfonyl
halide, an .alpha.-haloester, an .alpha.-halonitrile, an
.alpha.-haloketone, an imidylhalide, or combinations thereof.
4. A process according to claim 3, wherein said halogen is one or
more of chlorine, bromine, or iodine.
5. A process according to claim 4, wherein said catalyst is a
non-metal reducing, single electron transfer agent.
6. A process according to claim 5, wherein said catalyst is one or
more of SO.sub.2-containing compounds, including
Na.sub.2S.sub.2O.sub.4, H.sub.2NC(.dbd.NH)SO.sub.2H,
HOCH.sub.2SO.sub.2Na, HOCH.sub.2SO.sub.3Na, Na.sub.2SO.sub.3,
Na.sub.2S.sub.2O.sub.5, Na.sub.2S.sub.2O.sub.3, CH.sub.3SO.sub.2Na,
C.sub.6H.sub.5SO.sub.2Na, p-CH.sub.3C.sub.6H.sub.4SO.sub.2Na, or a
polydialkylamino-substituted unsaturated organic compound,
including (Me.sub.2N).sub.2C.dbd.C(NMe.sub.2).sub.2, or
combinations thereof.
7. A process according to claim 6, wherein said catalyst is present
in an amount of from about 0.01 to about 4 moles per mole of
initiating group in the initiator, and said catalyst is sodium
dithionite or formamidinesulfinic acid.
8. A process according to claim 5, wherein said initiator is
present in an amount from about 10,000 to about 1 moles of vinyl
chloride monomer per one mole of initiator and said vinyl chloride
monomer is vinyl chloride.
9. A process according to claim 6, including said buffer, wherein
said buffer includes one or more of NaHCO.sub.3, Na.sub.2HPO.sub.4,
NaH.sub.2PO.sub.4, CH.sub.3COONa, KHCO.sub.3, K.sub.2HPO.sub.4,
KH.sub.2PO.sub.4, CH.sub.3COOK, NH.sub.4HCO.sub.3,
(NH.sub.4).sub.2HPO.sub.4, NH.sub.4H.sub.2PO.sub.4,
CH.sub.3COONH.sub.4 or combinations thereof, and said buffer is
present in an amount from about 0.1 to about 5 moles of buffer per
mole of catalyst.
10. A process according to claim 1, further including said
comonomer, wherein said comonomer is an acrylate, a vinylidene
halide, a 2-haloalkene, a methacrylate, an acrylonitrile, a
methacrylonitrile, a vinyl halide, a styrene, an acrylamide, a
methacrylamide, a vinyl ketone, a N-vinylpyrrolidinone, a vinyl
acetate, a maleic acid ester or combinations thereof, and said
comonomer is present in an amount of from about 1% up to about
99%.
11. A process according to claim 10, wherein said comonomer is
vinylidene chloride, acrylonitrile, 2-chloropropene, acrylic acid
esters and maleic acid esters.
12. A process according to claim 1, comprising vinyl chloride, an
initiator containing one or more of a mono, di, tri or
polyfunctional .alpha.,.alpha.-dihaloalkane,
.alpha.,.alpha.,.alpha.-trihaloalkane, a perhaloalkane, a
perfloroalkyl halide, a benzyl halide, an allyl halide, a sulfonyl
halide, an .alpha.-haloester, an .alpha.-halonitrile, an
.alpha.-haloketone, an imidylhalide, or combinations thereof; a
catalyst containing one or more of SO.sub.2-containing compounds,
including Na.sub.2S.sub.2O.sub.4, H.sub.2NC(.dbd.NH)SO.sub.2H,
HOCH.sub.2SO.sub.2Na, HOCH.sub.2SO.sub.3Na, Na.sub.2SO.sub.3,
Na.sub.2S.sub.2O.sub.5, Na.sub.2S.sub.2O.sub.3, CH.sub.3SO.sub.2Na,
C.sub.6H.sub.5SO.sub.2Na, p-CH.sub.3C.sub.6H.sub.4SO.sub.2Na or a
polydialkylamino-substituted unsaturated organic compound including
(Me.sub.2N).sub.2C.dbd.C(NMe.sub.2).sub.2 and combinations thereof;
a buffer, wherein said buffer is one or more of NaHCO.sub.3,
Na.sub.2HPO.sub.4, NaH.sub.2PO.sub.4, CH.sub.3COONa, KHCO.sub.3,
K.sub.2HPO.sub.4, KH.sub.2PO.sub.4, CH.sub.3COOK,
NH.sub.4HCO.sub.3, (NH.sub.4).sub.2HPO.sub.4,
NH.sub.4H.sub.2PO.sub.4, CH.sub.3COONH.sub.4, and combinations
thereof; and an electron shuttle, wherein said shuttle is a
I,I'-dialkyl-4,4'-bipyridinium dihalide.
13. A process according to claim 4, wherein said halogen containing
initiator is part of a polymer chain, including the chain ends of
the said polymer.
14. A process according to claim 6, including said electron
shuttle, wherein said shuttle is a I,I'-dialkyl-4,4'-bipyrridinium
dihalide, and said electron shuttle is present in an amount from
about 0.00001 to about 1 mole of shuttle per mole of catalyst.
15. A process according to claim 14, including said surfactant,
wherein said surfactant is on or more of sodium dodecylsulfate,
hydroxypropyl methylcellulose, 72.5% hydrolyzed polyvinyl acetate,
polyoxyethylene (10) oleyl ether, polyoxyethylene (20) oleyl ether,
or combinations thereof, and said surfactant is present in an
amount from about 10 to about 5000 parts per million w/w relative
to halide containing monomer.
16. A process according to claim 1, wherein the molecular weight
distribution of said composition is from about .ltoreq.2.0 down to
about .ltoreq.1.5.
17. A process according to claim 6, wherein said molecular weight
distribution is from about .ltoreq.1.5 down to about
.ltoreq.1.1.
18. A process according to claim 6, wherein said vinyl chloride
monomer is dissolved in a solvent, said solvent comprising one or
more of halogenated benzenes, linear and cyclic ethers, ketones,
esters, alkanes, alcohols and combinations thereof, and wherein
said solvent is present in an amount from about 25 to about 1000
parts by weight per 100 parts by weight of the vinyl chloride
monomer.
19. A process according to claim 18, wherein said solvent is
chlorobenzene, dichlorobenzene, trichlorobenzene, xylene,
diphenylether, 1,2-dichloro ethane, tetrahydrofuran, dioxane,
dimethylformamide, cyclohexanone, acetone, diethyloxalate,
ethylhexylphtalate, dimethysulfoxide, methanol, ethanol, butanol or
combinations thereof, and said solvent is present in an amount from
about 1 to about 10 parts per volume of halide containing
monomer.
20. A process according to claim 1, wherein the polymerization of
said vinyl chloride monomer is carried out in water.
21. A process according to claim 6, wherein the polymerization of
said vinyl chloride monomer is carried out in mixtures of water
with chlorobenzene, dichlorobenzene, trichlorobenzene, xylene,
diphenylether, 1,2-dichloroethane, tetrahydrofuran, dioxane,
dimethylformamide, cyclohexanone, acetone, diethyloxalate,
ethylhexylphtalate, dimethysulfoxide, methanol, ethanol, butanol or
combinations thereof.
Description
BACKGROUND OF THE INVENTION
1.Field of the Invention
The present invention relates to the non-metal catalyzed radical
and living radical polymerization of halogen containing monomers
such as vinyl halides and vinylidene halides. In particular, this
invention relates to a process for the synthesis, in the presence
of a non-metallic catalyst, of poly(vinyl chloride) (PVC) with
controlled molecular weight and narrow molecular weight
distribution. The polymerization can be initiated from various
electron accepting radical precursors such as polyhalocarbons in
the presence of non-metal reducing single electron transfer
reagents as catalysts which can include low valent sulfur salts
containing SO.sub.2 group. The process can be accelerated by
electron shuttles such as alkyl viologens.
2. Description of the Prior Art
Heretofore, it was known to polymerize vinyl chloride (VC) and
other vinyl halide monomers using conventional free radical
processes. However, even in the presence of certain molecular
weight additives, there is limited control over the molecular
weight and polydispersity of the resulting polymer. In addition, VC
polymers are thermally unstable and require thermal stabilizers for
their practical use. Heretofore, there have been no methods
reported to prepare poly(vinyl chloride) by a non-metal-catalyzed
living process initiated from an active halide compound in which
the molecular weight and the molecular weight distribution of PVC
could be controlled.
Conventional free radical polymerization of vinyl chloride (VC) is
accompanied by the formation of thermally labile tertiary and
allylic chlorine defects which are responsible for the low thermal
stability of poly(vinyl chloride). This provides its most relevant
technological limitations. These structural defects are generated
during the conventional radical polymerization of VC and are
responsible for the initiation of a zipper mechanism of thermal
degradation of PVC.
In U.S. patent Ser. No. 09/893,201, which is herein fully
incorporated by reference, there is described a process for the
living radical polymerization of vinyl halides utilizing a metal
(preferably Cu) catalyst. The polymerization processes taught
therein include both non-aqueous high temperature and aqueous room
temperatures processes. The former gives polymers with low yields
(maximum 30%) and high molecular weight distribution up to about
1.7. The latter achieves high conversions and lower molecular
weight distribution (up to 1.50). Both processes show linear
molecular weight dependence on the monomer conversion. A single
electron transfer mechanism mediated by metals is proposed for the
initiation and dormant species activation steps
The PVC obtained by aqueous room temperature copper-catalyzed
living radical polymerization of vinyl chloride as described in
U.S. patent Ser. No. 09/893,201, contains a vanishingly small
amount of carbon-carbon double bonds in comparison with
conventional PVC. This allows us to consider such a polymer as one
free of at least allylic chlorine defects that could lead to new
properties. Alternatively, the use of heavy metal in polymerization
processes requires an additional utilization of the spent catalyst
and purification of the polymer, thereby increasing the cost.
Previously, attempts on living radical polymerization of vinyl
halides, which did not involve metal catalysis, were based on
degenerative chain transfer processes using iodine containing chain
transfer agents and peroxy-esters as initiators. As is taught in
U.S. Pat. No. 5,455,319, such a process was carried out at
temperatures conventionally used for vinyl halide polymerizations.
In addition, the polydispersity never decreased to values below
1.7
SUMMARY OF THE INVENTION
There has now been found a process for the polymerization of vinyl
chloride to form PVC polymers, and not telomers, utilizing a
metal-catalyzed radical and living radical polymerization. Various
activated mono, di, tri and multifunctional organic halide
initiators, including the allylic chlorines normally found in
chlorine containing polymers such as PVC, in conjunction with
certain metal catalysts, can successfully initiate the radical
polymerization of vinyl chloride. Optionally, a solvent or water or
mixtures thereof and a ligand for the metal catalyst can be
utilized in the polymerization of the vinyl chlorine monomer of the
present invention.
In a further embodiment, a method of polymerizing vinyl chloride to
form PVC polymers, and not telomers, has now been found utilizing
non-metal-catalyzed radical and living radical polymerization.
Various activated electron accepting radical precursor initiators,
such as polyhalocarbons, in conjunction with certain non-metallic
single electron donors as catalysts can successfully initiate the
radical polymerization of vinyl halide. The process occurs in water
or aqueous--organic solvent solutions. Optionally, an electron
shuttle such as an alkyl viologen, a surfactant, and a buffer can
be utilized in the polymerization of the vinyl halide monomer of
the present invention.
BRIEF DESCRIPTION OF THE DRAWINGS
FIG. 1 illustrates the dependence of the molecular weight (.lamda.,
.mu.) and molecular weight distribution (v, o) on conversion for
the metal catalyzed polymerization of vinyl chloride initiated from
-diiodo-p-xylene at 130.degree. C. in o-DCB ([VC]=4.8M). Closed
symbols: [VC]:[I]:[Cu(O)]:[bpy]=260:1:4:8; open symbols:
[VC]:[I]:[Cu(O)]:[bpy]=520:1:4:8
FIG. 2 illustrates the dependence of molecular weight (.sigma. and
molecular weight distribution (.nu.) on conversion for the
polymerization of VC initiated from CH.sub.3--CHCl--I and catalyzed
by Cu(O)/bpy in water at 90.degree. C. in the presence of sodium
dodecylsulfate (NaDDS).
[VC]:[CH.sub.3CHClI]:[Cu(O)]:[bpy]:[NaDDS]=100:1:2:4:0.5.
FIG. 3 illustrates the dependence of molecular weight, molecular
weight distribution and conversion on temperature and concentration
for the polymerization of VC initiated from CH.sub.3--CHCl--I and
catalyzed by Cu(O)/bpy in bulk and in o-DCB at 60.degree. C.
(.sigma., .tau.) 90.degree. C. (.nu.,.theta., +) and 130.degree. C.
(.lamda., .mu., 5).
[VC]:[CH.sub.3CHClI]:[Cu(O)]:[bpy]=100:1:2:4.
FIG. 4 illustrates the dependence of molecular weight (.lamda. and
molecular weight distribution (.sigma. on conversion for the
polymerization of VC initiated from CH.sub.3--CHCl--I and catalyzed
by Cu(O)/TREN in water at 20.degree. C. in the presence of sodium
dodecylsulfate (NaDDS).
[VC]:[CH.sub.3CHClI]:[Cu(O)]:[bpy]:[NaDDS]=100:1:2:4:0.5.
FIG. 5 illustrates Room Temperature Na.sub.2S.sub.2O.sub.4-mediated
LRP of VC Initiated with iodoform in H.sub.2O/THF.
[VC]/[CHI.sub.3]/[Na.sub.2S.sub.2O.sub.4]/[NaHCO.sub.3]=200/1/2/2.2
(mol/mol/mol/mol).
Left, the kinetic plot, conversion (open symbols) and concentration
logarithm (closed symbols) on time. Right, the dependence of the
number average molecular weight (closed symbols) and molecular
weight distribution (open symbols) on theoretical number average
molecular weight.
FIG. 6 illustrates Room Temperature Na.sub.2S.sub.2O.sub.4-mediated
LRP of VC Initiated with iodoform in H.sub.2O/THF in the presence
of surfactant Brij.RTM. 98.
[VC]/[CHI.sub.3]/[Na.sub.2S.sub.2O.sub.4]/[NaHCO.sub.3]/[Brij.RTM.
98]=200/1/2/2.2/2080 (mol/mol/mol/mol/mol/ppm w/w to VC).
Left, the kinetic plot, conversion (open symbols) and concentration
logarithm (closed symbols) on time. Right, the dependence of the
number average molecular weight (closed symbols) and molecular
weight distribution (open symbols) on theoretical number average
molecular weight.
FIG. 7 illustrates Room Temperature Na.sub.2S.sub.2O.sub.4-mediated
LRP of VC Initiated with iodoform in H.sub.2O/THF in the presence
of electron shuttle OV.sup.2+ and surfactant Brij.RTM. 98.
[VC]/[CHI.sub.3]/[Na.sub.2S.sub.2O.sub.4]/[NaHCO.sub.3]/[OV.sup.2+]/[Brij-
.RTM. 98]=200/1/2/2.2/0.00175/2080 (mol/mol/mol/mol/mol/ppm W/W to
VC).
Left, the kinetic plot, conversion (open symbols) and concentration
logarithm (closed symbols) on time. Right, the dependence of the
number average molecular weight (closed symbols) and molecular
weight distribution (open symbols) on theoretical number average
molecular weight.
FIG. 8 illustrates Room Temperature Na.sub.2S.sub.2O.sub.4-mediated
LRP of VC Initiated with iodoform in H.sub.2O/THF in the presence
of electron shuttle MV.sup.2+ and surfactant Brij.RTM. 98.
[VC]/[CHI.sub.3]/[Na.sub.2S.sub.2O.sub.4]/[NaHCO.sub.3]/[MV.sup.2+]/[Brij-
.RTM. 98]=200/1/2/2.2/0.00175/2080 (mol/mol/mol/mol/mol/ppm w/w to
VC).
Left, the kinetic plot, conversion (open symbols) and concentration
logarithm (closed symbols) on time. Right, the dependence of the
number average molecular weight (closed symbols) and molecular
weight distribution (open symbols) on theoretical number average
molecular weight.
FIG. 9 illustrates Room Temperature
Na.sub.2S.sub.2O.sub.8--HCOONa-mediated radical polymerization of
VC initiated with bromoform in H.sub.2O/THF.
[VC]/[CHBr.sub.3]/[Na.sub.2S.sub.2O.sub.8]/[HCOONa]/[NaHCO.sub.3]=200/1/2-
/2/2.2 (mol/mol/mol/mol/mol).
Left, the kinetic plot, conversion (open symbols) and concentration
logarithm (closed symbols) on time. Right, the dependence of the
number average molecular weight (closed symbols) and molecular
weight distribution (open symbols) on theoretical number average
molecular weight.
FIG. 10 illustrates Room Temperature
Na.sub.2S.sub.2O.sub.8--HCOONa-medicated radical polymerization of
VC initiated with chloroform in H.sub.2O/THF.
[VC]/[CHBr.sub.3]/[Na.sub.2S.sub.2O.sub.8]/[HCOONa]/[NaHCO.sub.3]=200/1/2-
/2/2.2 (mol/mol/mol/mol/mol).
Left, the kinetic plot, conversion (open symbols) and concentration
logarithm (closed symbols) on time. Right, the dependence of the
number average molecular weight (closed symbols) and molecular
weight distribution (open symbols) on theoretical number average
molecular weight.
FIG. 11 illustrates Room Temperature
H.sub.2NC(.dbd.NH)SO.sub.2H-mediated LRP of VC initiated with
iodooform in H.sub.2O/THF in the pesence of electron shuttle
OV.sup.2+.
[VC]/[CHI.sub.3]/[H.sub.2NC(.dbd.NH)SO.sub.2H]/[NaHCO.sub.3]/[OV.sup.2+]=-
200/1/2/4.4/0.0035 (mol/mol/mol/mol/mol).
Left, the kinetic plot, conversion (open symbols) and concentration
logarithm (closed symbols) on time. Right, the dependence of the
number average molecular weight (closed symbols) and molecular
weight distribution (open symbols) on theoretical number average
molecular weight.
DETAILED DESCRIPTION OF THE INVENTION
In the metal-catalyzed polymerization of chlorine containing
monomers, appropriate initiators include halides and pseudohalides
of the formula R--X, where R having from 1 to 100,000 carbon atoms,
contains an activating electron withdrawing group such as cyano,
ester, perfloroalkyl or any other unit capable of stabilizing a
radical such as benzyl or allyl, and X=halide. The halide
initiators include, but are not limited to various activated mono,
di, tri and polyfunctional .alpha.,.alpha.-dihaloalkanes,
.alpha.,.alpha.,.alpha.-trihaloalkanes, perhaloalkanes,
perfloroalkyl halides, benzyl halides, allyl halides, sulfonyl
halides, .alpha.-haloesters, .alpha.-halonitriles,
.alpha.-haloketones, imidyl halides, or combinations thereof.
Additionally, any compound having labile carbon-halide,
nitrogen-halide, sulfur-halide, phosporus-halide, silicon-halide
bonds which can dissociate homolytically by themselves or in the
presence of a metal catalyst are suitable for use as initiators in
the present invention. Suitable structures for initiators utilized
in the present invention are set forth in Scheme 3.
Generally, preferred initiators include chlorine, bromine and
thiocyanate containing compounds, with iodide initiators being
desirable. Mono, di and trifunctional .alpha.-haloesters act as
active initiators for the polymerization of vinyl chloride in the
presence of Fe(O), TiCp.sub.2Cl.sub.2 and Cu(O) and its salts such
as Cu.sub.2Te, Cu.sub.2Se, Cu.sub.2S, Cu.sub.2O, CuCl, CuBr, Cul
and copper thiophenoxide (CuSPh), copper butanethiolate (CuSBu),
copper phenylacetylide (CuC.dbd.CPh). Various chlorine containing
initiators such as CH.sub.3CH(CN)Cl, Cl--CH.sub.2-Ph-CH.sub.2--Cl
or R--CH.dbd.CH--CH.sub.2--Cl and R--SO.sub.2--Cl also promote the
polymerization of chlorine containing monomers in the presence of
catalysts such as Cu(O) and its salts, Fe(O) and
TiCp.sub.2Cl.sub.2. The preferred initiators that lead to polymers
of narrowest molecular weight distribution in the presence of Cu(O)
and its salts or complexes are the active iodine containing
substrates of the type R.sub.1R.sub.2R.sub.3C--I where at least one
of the R substituents is an electron withdrawing group (EWG) or
radical stabilizing group such as benzylic, allylic, .alpha.-halo,
.alpha.-cyano, .alpha.-ester, .alpha.-trifluoromethyl and so on.
The other R substituents can be H, alkyl chains including polymer
chains, electron withdrawing groups and combinations thereof. The
preferred iodine containing initiators include:
I--CH.sub.2-Ph-CH.sub.2--I, CH.sub.3--CH(Cl)--I, CH.sub.2I.sub.2,
CHI.sub.3, Cl.sub.4, CH.sub.2.dbd.CH--CH.sub.2--I,
CF.sub.3--(CF.sub.2).sub.n--I, I--CH.sub.2--CONH.sub.2 and
I--CH.sub.2--COO--(CH.sub.2).sub.n--H (n=1 20).
##STR00001## ##STR00002##
The amounts of such halide initiators utilized depend on the
desired molecular weight of the halide containing polymer and are
generally from about 5,000 to about 10, desirably from about 1000
to about 25, and preferably from about 500 to about 50 moles of
halide containing monomer per one mole of initiating group.
Generally the number average molecular weight of the halide
containing polymer will be from about 500 to about 100,000,
desirably from about 1000 to about 60,000, and preferably from
about 3,000 to about 40,000.
The chlorine-containing monomers which are polymerized or
copolymerized according to this invention are vinyl chloride and
its structurally related derivatives and monomers known to
copolymerize via a radical mechanism with vinyl chloride, including
vinylidene chloride and 2-chloropropene. The preferred carbon atom
range of each group of monomers is from 2 to 20. The copolymer can
have a comonomer content from 1% up to 99%, depending on the
reactivity ratios of the comonomers used.
A metal species is utilized to catalyze the initiation reaction and
continue the growth of the polymer chain. Typical radical forming
catalysts include metal-based catalysts, as metals and/or salts
thereof. Examples of such catalysts include metals in their zero
oxidation state such as copper, iron, aluminum, cadmium, zinc,
samarium, chromium, molybdenum, manganese, tungsten, cobalt,
nickel, rhodium, ruthenium, palladium, titanium and certain higher
valence salts thereof. The preferred catalyst will be dependent
upon the initiator utilized and on the reaction media (such as
solvent or water) and temperature. While the initiation step
(addition of the radical fragment derived from the initiator to
vinyl chloride) may be achieved with all catalysts, it is preferred
that the metals be in their zero oxidation state for the metal
catalyzed propagation and therefore, living radical polymerization
to occur. Additionally, the catalyst may be a mixture of two or
more metals in their zero oxidation state, a metal salt or complex,
a mixture of two or more metal salts or complexes, or a mixture of
two or more metals in their zero oxidation state with metal salts
or complexes. Preferred catalysts include Cu(O), copper sulfide
(Cu.sub.2S), copper selenide (Cu.sub.2Se), copper teluride
(Cu.sub.2Te) copper thiophenoxide (CuSPh), copper butanethiolate
(CuSBu), copper phenylacetylide CuC.dbd.CPh, Fe(O), and titanium
cyclopentadienyl dichloride (TiCp.sub.2Cl.sub.2)
It has been found that Cu(O) is able to generate polymers
regardless of the nature of the halide in the initiator. When Fe(O)
is used as catalyst for the polymerization of vinyl chloride, it
has been found that chlorine and bromine based initiators are
suitable. The preferred initiators for Fe(O) are for example, the
active (CH.sub.3).sub.2(COOEt)--Br, CH.sub.3--CH(Ph)--Br,
F-Ph-SO.sub.2--Cl, as well as the
--CH.sub.2--(CH.sub.3)C(COOMe)--Cl chain end of PMMA synthesized by
metal catalyzed living radical polymerization. For titanium-based
catalysts such as TiCp.sub.2Cl.sub.2, chlorine containing
initiators such as Cl--CH.sub.2-Ph-CH.sub.2--Cl and
CH.sub.3CH(CN)--Cl or CH.sub.2.dbd.CH--CH.sub.2--Cl are
particularly suitable.
The amount of catalyst is dependent upon the desired reaction rate.
Generally, the amount of catalyst will be from about 0.01 to about
10 desirably from about 0.75 to about 4, and preferably from about
1 to about 3 moles per mole of halide in the initiator.
A ligand can optionally be included in the polymerization reaction
in order to aid in the solubilization of the catalyst. The ligand
used will depend specifically and uniquely on the type of catalyst,
the temperature of the reaction and on the reaction media such as
solvent or water. The ligand can be any organic species capable of
complexing the metal in its zero oxidation state and in its higher
oxidation states. For Cu-based catalysts, the ligands can include
basic aromatic and aliphatic nitrogen and phosphorus containing
compounds such as 2,2'-bipyridyl (bpy) and its 4,4'-alkyl
substituted compounds such as 4,4'-dinonyl-2,2'-bipyridyl (bpy-9),
pentamethylene diethyl triamine, (PMDETA), tris(2-aminoethyl)amine
(TREN), tris[2-(dimethylamino)ethyl]amine (Me.sub.6-TREN),
triphenylphosphine, triphenylphosphine oxide, and combinations
thereof. The foregoing ligands and 1,10-phenantroline are also
appropriate for Fe-based catalysts. In addition, other ligands such
as CO, acetylacetonate, or terpyridine may be used. The use of a
ligand is not necessary for TiCp.sub.2Cl.sub.2 but is preferred for
Cu and Fe based catalysts.
When the optional ligand is present, the mixture will usually
contain from about 0.1 to about 10 moles of ligand per mole of
catalyst, desirably from about 0.75 to about 3 moles of ligand per
mole of catalyst, and preferably from about 1 to about 2 moles of
ligand per mole of catalyst.
Additionally, various additives may optionally be utilized in the
polymerization. Depending on their structure, these additives may
affect the molecular weight and molecular weight distribution of
the resulting polymer. Such additives can include sodium iodide,
urea, Al.sup.iBu.sub.3, Ti(OBu).sub.4 and 2,6-di-tertbutyl-4-methyl
pyridine, with 2,6-di-tertbutyl-4-methyl pyridine being preferred
and may be added in a similar molar amount as the initiator.
Polymerization of the chlorine containing monomer is usually
carried out in the presence of the catalyst and initiator in a
closed vessel in an inert atmosphere such as nitrogen, or argon;
under autogenous or artificially-induced pressure. The temperature
of the polymerization can vary widely depending upon the type of
initiator and/or catalyst, but is generally from about 0.degree. C.
to about 180.degree. C., desirably from about 10.degree. C. to
about 150.degree. C. and preferably from about 20.degree. C. to
about 130.degree. C. It has been found that lower temperatures,
i.e., 20.degree. C. 90.degree. C., depending on the initiator and
catalyst system, lead to lower reaction rates, and higher molecular
weight polymers. For solution polymerizations, the Cu(O)/bpy
catalyst in conjunction with the X--CH.sub.2-Ph-CH.sub.2--X (X=Cl,
Br, I, SCN) or CHI.sub.3 and Cl.sub.4 initiators are effective only
at about 120.degree. C. and above, while other chlorine, bromine
and iodine based initiators generate polymers at temperatures as
low as 60.degree. C. This temperature is enough to allow the metal
catalyzed reinitiation from chain such as --CH(Cl)--X (X=I, Br,
Cl). Higher temperatures promote an increase in the rate of all
reactions including chain transfer to monomer. Therefore, a
preferred catalyst will be one reactive enough to promote
reinitiation from the active halide chain ends at lower
temperatures or to successfully compete with chain transfer to
monomer at high temperatures.
Optionally, appropriate solvents such as organic fluids or mixtures
of organic fluids may be utilized. Naturally, solvents which do not
interfere with the reaction are used and suitable solvents include
organic solvents such as chlorobenzene, dichlorobenzene,
trichlorobenzene, xylene, diphenylether, 1,2-dichloro ethane,
dimethylformamide (DMF), tetrahydrofuran (THF), dioxane,
dimethylsulfoxide, (DMSO) ketones or esters or any of the other
solvents and plasticisers for PVC and their copolymers known in the
literature and to those skilled in the art. The amount of solvent
used depends on the desired solubility of the system, on the
temperature and the desired pressure in the reaction vessel and can
be easily determined by one skilled in the art. The amount of
solvent generally ranges from about 25 to about 1000, desirably
from about 50 to about 500, and preferably from about 75 to about
400 parts per 100 parts of halide containing monomer, such as vinyl
chloride.
Alternatively, it has been found that the living free radical
polymerization of vinyl chloride can be carried out in the absence
of solvent. In such situations, the polymerization is generally
carried out in bulk and the other reaction conditions set forth
hereinabove are generally suitable.
Alternatively, it has also been found that the living radical
polymerization of vinyl chloride can be carried out in water and in
water/organic solvent mixtures using the aforementioned solvents as
well as other solvents. The presence of an emulsifier such as
sodium dodecylsulfate (NaDDS) is optional. The aforementioned
conditions still apply. In addition, it was also found that the
Cu(O)/TREN, Cu.sub.2Y/TREN (Y=O, S, Se, Te), and CuX/TREN (X=Cl,
Br, I, SPh, SBu, C.dbd.CPh) catalyst and ligand systems or mixtures
thereof can successfully catalyze VC polymerization initiated from
iodo, bromo or chloro containing initiators to complete conversion
at room temperature. The amount of the optional emulsifier depends
of the desired particle size, nature of the emulsifier, and the
water to monomer ratio and can be easily selected by one skilled in
the art.
Depending on the desired properties of the homopolymer or
copolymer, the polymerizations can be either batch, semi-batch or
continuous. Mechanical agitation is desirable, but not necessary.
Normal polymerization time depends on the temperature and the
monomer to initiator to catalyst to ligand ratios and is from 0.5
to about 24 hours.
Subsequent to the formation of the polymer composition, solvent and
excess monomer are removed, for example by evaporation,
precipitation of the polymer, and the like.
In a second embodiment, in the aqueous room temperature
non-metal-catalyzed polymerization of halogen containing monomers,
appropriate initiators include halides of the formula RX, where R,
having 1 1, 000 carbon atoms, contains an activated electron
withdrawing group such as a halogen, polyhalo, or perfluoroalkyl,
and X--halide (where X.sup.- is a good living group and X=Cl, Br,
I). The halide initiator can accept one electron and then release
X.sup.- forming an initiating radical R.
##STR00003## Such electron-accepting radical precursors include,
but are not limited to, various activated mono, di, tri and
polyfunctional activated halides. These include
.alpha.,.alpha.-dihaloalkanes,
.alpha.,.alpha.,.alpha.-trihaloalkanes, perhaloalkanes,
perfluoroalkyl halides, polyfluoroalkyl halides,
.alpha.-haloesters, .alpha.-halonitriles, .alpha.-haloketones,
benzyl halides, sulfonyl halides, imidyl halides, or combinations
thereof. Additionally, any compounds having labile carbon-halide,
nitrogen-halide, phosphorus-halide, silicon-halide bonds, which
possess enough electron affinity to accept one electron and then
release halide-anion forming radicals, are suitable for use as
initiators in the present invention, and can include, for example,
benzyl iodide, N-iodosuccinimide, diphenylposphinic iodide,
triphenylsilyl iodide, and the like.
Generally, preferred initiators are one electron accepting radical
precursors including chlorine and bromine, with iodine initiators
being desirable. Haloforms, tetrahalocarbons, methylene iodide,
1-chloro-1-iodo-ethane, as well as PVC's obtained from them, act as
active initiators in conjunction both with Na.sub.2S.sub.2O.sub.4,
H.sub.2NC(.dbd.NH)SO.sub.2H, which give the highest efficiency, and
also HOCH.sub.2SO.sub.2Na, HOCH.sub.2SO.sub.3Na, Na.sub.2SO.sub.3,
Na.sub.2S.sub.2O.sub.5, Na.sub.2S.sub.2O.sub.3, CH.sub.3SO.sub.2Na,
C.sub.6H.sub.5SO.sub.2Na, p-CH.sub.3C.sub.6H.sub.4SO.sub.2Na,
(Me.sub.2N).sub.2C.dbd.C(NMe.sub.2).sub.2. It should be noted that
the system sodium persulfate--sodium formate
(Na.sub.2S.sub.2O.sub.8--HCOONa, which form CO.sub.2.sup.- radical
anion) is active in radical (not living) polymerization of vinyl
chloride in conjunction with only non-iodine containing halocarbon
initiators--CHCl.sub.3, CHBr.sub.3 (FIGS. 9, 10), CCl.sub.4,
CBr.sub.4. Whereas, in conjunction with CHI.sub.3, the
persulfate-formate system is not effective at all due to evolution
of I.sub.2 which terminates the polymerization. Preferred
initiators include iodoform, 1-chloro-1-iodoetane, and
1-iodoperfluoroalkane.
The amounts of the initiators utilized depend on the desired
molecular weight of the halide containing polymer and are generally
from about 5000 to about 1, desirably from about 1000 to about 10,
and preferably from about 500 to about 50 of halide containing
monomer per mole of initiating group. Generally the number average
molecular weight of the halide containing polymer will be from
about 500 to about 60,000, desirably from about 1,000 to about
40,000, and preferably from about 2,000 to about 20,000.
The vinyl halide monomers which are polymerized or copolymerized
according to this invention are vinyl chloride and its structurally
related derivatives, including vinylidene chloride and
2-chloropropene and monomers known to copolymerize via a radical
mechanism with vinyl chloride, including one or more of acrylates,
vinylidene halides, methacrylates, acrylonitrile,
methacrylonitrile, vinyl halides, 2-haloalkenes, styrenes,
acrylamide, methacrylamide, vinyl ketones, N-vinylpyrrolidinone,
vinyl acetate, maleic acid esters, or combinations thereof. The
preferred carbon atom range of each group of monomers is from 2 to
20. The copolymer can have a comonomer content from 1% up to 99%,
depending on the reactivity ratios of the comonomers used.
An important component of the second embodiment is the use of a
non-metallic single electron transfer species to catalyze the
initiation reaction and continue the growth of the polymer chain.
Typical of such catalysts are, for example, low valent sulfur salts
containing SO.sub.2 group and polydialkylamino-substituted
unsaturated organic compounds. Examples of such catalysts include
Na.sub.2S.sub.2O.sub.4, H.sub.2NC(.dbd.NH)SO.sub.2H,
HOCH.sub.2SO.sub.2Na, HOCH.sub.2SO.sub.3Na, Na.sub.2SO.sub.3,
Na.sub.2S.sub.2O.sub.5, Na.sub.2S.sub.2O.sub.3, CH.sub.3SO.sub.2Na,
C.sub.6H.sub.5SO.sub.2Na, p-CH.sub.3C.sub.6H.sub.4SO.sub.2Na,
(Me.sub.2N).sub.2C.dbd.C(NMe.sub.2).sub.2, and the like. The
preferred catalyst will be dependent upon the initiator utilized
and on the reaction media (such as solvent or water) and
temperature. Preferred catalysts include sodium dithionite
(Na.sub.2S.sub.2O.sub.4) and formamidinesulfinic acid
(H.sub.2NC(.dbd.NH)SO.sub.2H).
The amount of catalyst is dependent upon the desired reaction rate.
Generally, the amount of catalyst will be from about 0.01 to about
4, desirably from about 0.05 to about 2, and preferably from about
0.1 to about 1 mole per mole of initiator.
A buffer compound can optionally be included in the polymerization
process in order to avoid acidic decomposition of sulfur containing
catalysts. The buffer used will depend specifically and uniquely on
the type of catalyst, the temperature of the reaction and on the
reaction media such as solvent or water. Typical buffers can
include alkaline salts of inorganic and organic acids, which water
solutions keep pH 8 10, such as NaHCO.sub.3, Na.sub.2HPO.sub.4,
NaH.sub.2PO.sub.4, CH.sub.3COONa or the potassium or ammonium salts
thereof, including KHCO.sub.3, K.sub.2HPO.sub.4, KH.sub.2PO.sub.4,
CH.sub.3COOK, NH.sub.4HCO.sub.3, (NH.sub.4).sub.2HPO.sub.4,
NH.sub.4H.sub.4PO.sub.4, CH.sub.3COONH.sub.4, and the like.
When the optional buffer is present, the mixture will usually
contain from about 0.1 to about 5 moles of buffer per mole of
catalyst, desirably from about 0.5 to about 3 moles of buffer per
mole of catalyst, and preferably from about 1 to about 1.2 moles of
buffer per mole of catalyst.
The presence of an electron shuttle is also optional. The shuttle
allows for acceleration of the process of radical initiation and
activation of dormant species by using compounds which, in reduced
form are more soluble in organic phase than in water, and which in
oxidized form are more soluble in water than in organic solvent. In
a reduced state in the aqueous phase (having gained an electron),
the compound moves into the organic phase and donates an electron
to the halogen-containing initiator or dormant species. The
compound then returns to the aqueous phase carrying the halide
anion and leaving a radical in the organic phase. Such compounds
can include 1,1'-dialkyl-4,4'-bipyridinium dihalides called alkyl
viologens. Examples of such shuttles include, but are not limited
to, 1,1'-dimethyl-4,4'-bipyridinium dichloride, methyl viologen
(MV.sup.2+), 1,1'-di-n-octyl-4,4'-bipyridinium dibromide, octyl
viologen (OV.sup.2+), and the like.
When the shuttle is present, the mixture will usually contain from
about 0.00001 to about 1 moles of shuttle per mole of catalyst,
desirably from about 0.0001 to about 0.01 moles of shuttle per mole
of catalyst, and preferably from about 0.001 to about 0.005 moles
of shuttle per mole of catalyst.
Additionally, various additives may optionally be utilized in the
polymerization. Depending on their structure, these additives may
affect the molecular weight, molecular weight distribution of the
resulting polymer, catalyst stability and/or rate of
polymerization. Such additives can include sodium iodide, ammonium
iodide, tetrabutyl ammonium iodide, and sodium chloride. These can
be added in similar amounts as the initiators.
The non-metallically catalyzed polymerization reactions described
herein are normally carried out in the presence of catalyst and
initiator in a closed vessel in an inert atmosphere such as
nitrogen or argon, under autogenously or artificially induced
pressure. The optimal temperature of the polymerization is around
room temperature, namely 25.degree. C..+-.5.degree. C. A higher
temperature can lead to fast reduction of active chain ends and a
lower one is simply inconvenient due to necessity to use special
cooling equipment. This can lead to higher viscosity, heterogeneity
and reduced solubility of reaction components that make results
less reproducible.
Appropriate solvents such as water or a mixture of water and
organic solvent may be utilized. Solvents play an important role in
single electron transfer. It was found that there is no reaction in
the absence of water when salts are used. The higher the solvent
polarity is, the more efficient is the polymerization. By this
means, polar water-soluble organic solvents and good PVC solvents
such as tetrahydrofuran (THF), dimethylformamide (DMF),
dimethylsulfoxide (DMSO), cyclohexanone, chlorobenzene,
dichlorobenzene, trichlorobenzene, xylene, diphenylether,
1,2-dichloroethane, dioxane, acetone, diethyloxalate,
ethylhexyphtalate, methanol, ethanol, butanol, or combinations
thereof, or any other solvent in the literature known to those
skilled in the art are appropriate media for the polymerization.
The amount of the solvent generally ranges from 1 to 10 parts per
volume of halide containing monomer and preferably is from about 2
to about 4 parts per volume (ppv).
The presence of a surfactant is optional. Examples of the
surfactants include, but are not limited to, sodium dodecylsulfate
(NaDDS), hydroxypropyl methylcellulose (Methocel.RTM. F50), 72.5%
hydrolyzed polyvinyl acetate (Alcotex.RTM. 72.5),
polyoxyethylene(10) oleyl ether (Brij.RTM. 97), and
polyoxyethylene(20) oleyl ether (Brij.RTM. 98). The amount of the
optional surfactant depends on the desired particle size, nature of
the surfactant and the water to monomer ratio. This can be easily
selected by one skilled in the art. The amount of surfactant
generally ranges from about 0.1 to about 50000 parts per million
(ppm) w/w, desirably from about 1 to about 10000 ppm w/w, and
preferably from about 10 to about 5000 parts per million w/w
relative to halide containing monomer.
Depending on desired properties of the homopolymer or copolymer,
the polymerization can be batch or semi batch, or continuous.
Mechanical agitation is desirable to obtain reproducible results,
but not necessary. Normal polymerization time depends on the
monomer--initiator ratio and desirable polymer properties and can
be from about 1 h to about 70 h.
Subsequent to the formation of the polymer composition, solvent and
excess monomer is removed, for example by evaporation of the vinyl
chloride and the addition of methanol to precipitate the
polymer.
An advantage of the living radical polymerization process described
herein is that it will produce a halogen-containing polymer, such
as PVC, with controlled molecular weight, such that the molecular
weight increases with the conversion of the monomer. Additionally,
the living radical polymerization process will provide PVC with
narrow molecular weight distribution and with the well defined
chain ends, i.e. telechelics and macromonomers. Such molecular
weight distribution, i.e. M.sub.w/M.sub.n, can be from
.ltoreq.2.00, .ltoreq.1.90, or .ltoreq.1.80 down to .ltoreq.1.70,
.ltoreq.1.60, or even .ltoreq.1.50. A molecular weight distribution
of from about .ltoreq.1.70 to about .ltoreq.1.50 is preferred and
less than 1.50 is most preferred. Since the structural defects in
PVC are responsible for its low thermal stability, PVC obtained by
living radical polymerization will be more stable than conventional
PVC, thereby expanding the range of technological applications of
PVC.
The poly(vinyl chloride) compositions described herein can be
useful for many applications including plastic materials (sheeting,
films, molded parts, etc.), viscosity/flow modifiers, additives for
flame retardant compositions, and compatibilizers.
The following examples show ways in which the invention can be
practiced, as well as comparative examples. However, the examples
do not limit the invention.
TABLE-US-00001 TABLE 1 Polymerization of Vinyl Chloride Initiated
from Various Halides and Catalyzed by Fe(0). Conv. Mw/ Temp Exp
Initiator Catalyst/Ligand [VC]:[I]:[C]:[L].sup.a) Time h % Mn Mn
.degree. C. Solvent 1 Br--(CH.sub.3).sub.2C(COOEt) Fe(0)/Phen
65:1:0.6:1 19 26 10,000 1.66 90 oDCB 2 Br--(CH.sub.3).sub.2C(COOEt)
Fe(0)/Phen 130:1:1.2:2 22 19 7,000 1.75 90 - THF 3
Br--(CH.sub.3).sub.2C(COOEt) Fe(0)/Phen 130:1:1.2:2.4 22 16 7,200
1.85 9- 0 DMF 4 Br--(CH.sub.3).sub.2C(COOEt) Fe(0)/Phen 130:1:1.2:2
40 15 19,100 1.65 60- oDCB 5 Br--(CH.sub.3).sub.2C(COOEt)
Fe(0)/Phen 130:1:1.2:2.4 22 30 10,200 1.73 - 90 oDCB 6
Br--(CH.sub.3).sub.2C(COOEt) Fe(0)/Phen 130:1:1.2:2.4 22 33 8,300
1.85 1- 30 oDCB 7 Br--(CH.sub.3).sub.2C(COOEt) Fe(0)/Phen
120:1:1.2:2.4: 20 42 9,000 1.75 - 90 oDCB 8
Br--(CH.sub.3).sub.2C(COOEt) Fe(0)/Phen/Al.sup.iBu.sub.3
130:1:1.2:2:1.2- 22 10 12,900 1.59 90 oDCB 9
Cl--(CH.sub.3)C(COOMe)-- Fe(0)/Phen 450:1:4.5:3.5 22 35 8,300 1.73
90 oD- CB --CH.sub.2-PMMA 10 Br--C(CH.sub.3).sub.2--CO--O--Ph--
Fe(0)/Phen 130:1:2:4 96 36 8,400 1.7- 5 90 oDCB
--Ph--OCO--C(CH.sub.3).sub.2--Br 11 Br--CH(Ph)CH.sub.3 Fe(0)/Phen
130:1:1.2:2 19 27 12,500 1.75 90 oDCB 12
Br--CH.sub.2--Ph--CH.sub.2--Br Fe(0)/Phen 130:1:1.2:2.4 22 10
13,300 1.- 5 90 oDCB 13 Br--CH.sub.2--Ph--CH.sub.2--Br Fe(0)/Phen
130:1:2:4 96 5 2,600 1.96 90 - oDCB 14
Cl--CH.sub.2--Ph--CH.sub.2--Cl Fe(0)/Phen 130:1:2:4 96 5 8,300 1.65
90 - oDCB 15 I--CH.sub.2--Ph--CH.sub.2--I Fe(0)/Phen 130:1:2:4 23
10 4,300 1.98 130 - oDCB 16 NCS--CH.sub.2--Ph--CH.sub.2--SCN
Fe(0)/Phen 130:1:2:4 48 8 4.800 1.90 9- 0 oDCB 17
Cl--(CN)CHCH.sub.3 Fe(0)/Phen 130:1:1.2:2.4 19 10 9,400 1.61 90
oDCB 18 Cl--(CN)CHCH.sub.3 Fe(CO).sub.5 130:1:1.2 18 4 14,300 1.65
90 oDCB 19 Cl--SO.sub.2--Ph--F Fe(0)/Phen 130:1:1.2:2.4 18 22 7,600
1.82 90 oDCB .sup.a)Molar ratio of VC to initiator to catalyst to
ligand
TABLE-US-00002 TABLE 2 Polymerization of Vinyl Chloride initiated
from Various Halides and Catalyzed by TiCp.sub.2Cl.sub.2. Conv Mw/
Temp Exp Initiator Catalyst/Additive [VC]:[I]:[C]:[A].sup.a) Time h
% Mn Mn .degree. C. Solvent 20 -- TiCp.sub.2Cl.sub.2 130:0:1 20 3
12,000 1.67 70 oDCB 21 Br--(CH.sub.3).sub.2C--COOEt
TiCp.sub.2Cl.sub.2 130:1:1.2 22 10 15,000 - 1.78 90 oDCB 22
Br--(CH.sub.3).sub.2C--COOEt TiCp.sub.2Cl.sub.2 130:1:1.2 20 7
21,400 1- .68 60 oDCB 23 Br--(CH.sub.3).sub.2C--COOEt
TiCp.sub.2Cl.sub.2/Al.sup.iBu.sub.3 130:1:- 1.2:3.6 17 60 3,800
2.10 90 oDCB 24 Br--(CH.sub.3).sub.2C--COOEt
TiCp.sub.2Cl.sub.2/Zn/bpy 130:1:1.2:1.8:0.- 7 22 22 14,800 1.95 90
oDCB 25 Br--(CH.sub.3).sub.2C--COOEt Ti(OBu).sub.4/Al.sup.iBu.sub.3
130:1:1.2:3- .6 17 87 5,300 1.80 90 oDCB 26
Br--C(CH.sub.3).sub.2--CO--O--Ph-- TiCp.sub.2Cl.sub.2 520:1:2 20 5
3,10- 0 2.05 130 oDCB Ph--OCO--C(CH.sub.3).sub.2--Br 27
Br--C(CH.sub.3).sub.2--OCO--Ph--C(CH.sub.3)-- TiCp.sub.2Cl.sub.2
520:1:- 2 20 7 4,400 1.81 130 oDCB
[(Ph--OCO--C(CH.sub.3).sub.2--Br].sub.2 28
Br--CH.sub.2--Ph--CH.sub.2--Br TiCp.sub.2Cl.sub.2 520:1:2 20 5
3,600 1.- 86 130 oDCB 29 Cl--CH.sub.2--Ph--CH.sub.2--Cl
TiCp.sub.2Cl.sub.2 520:1:2 20 28 4,900 1- .81 130 oDCB 30
Cl--CH.sub.2--Ph--CH.sub.2--Cl TiCp.sub.2Cl.sub.2 520:1:2 96 38
10,600 - 1.80 90 oDCB 31 NCS--CH.sub.2--Ph--CH.sub.2--SCN
TiCp.sub.2Cl.sub.2 260:1:3.5 22 5 4,00- 0 2.05 130 oDCB 32
Cl--CH(CN)CH.sub.3 TiCp.sub.2Cl.sub.2 130:1:1.2 19 22 16,000 1.72
90 oD- CB 33 Br--N(CO--CH.sub.2--CH.sub.2--CO) TiCp.sub.2Cl.sub.2
130:1:1.2 19 4 19,- 000 1.75 90 oDCB 34 Cl.sub.3(--NCO--).sub.3
TiCp.sub.2Cl.sub.2 390:1:2.1 20 5 8,200 1.80 90- oDCB 35
(Cl--SO.sub.2--Ph).sub.3C--CH.sub.3 TiCp.sub.2Cl.sub.2 400:1:9 22 7
4,0- 00 2.05 110 oDCB 36 Cl--SO.sub.2--Ph--F TiCp.sub.2Cl.sub.2
130:1:1.2 19 22 12,000 1.65 90 o- DCB .sup.a)Molar ratio of VC to
initiator to catalyst to additive
TABLE-US-00003 TABLE 3 Polymerization of Vinyl Chloride Initiated
from Various Halides and Catalyzed by Cu(I). Temp Exp Initiator
Catalyst/Ligand [VC]:[I]:[C]:[L].sup.a) Time h Mn Mw/Mn Conv %
.degree. C. Solvent 37 Br--C(CH.sub.3).sub.2--CO--O--Ph--
CuBr/Me.sub.6-TREN 260:1:4:8 20 2,50- 0 1.45 8 130 oDCB
Ph--O--CO--C(CH.sub.3).sub.2--Br 38
Br--C(CH.sub.3).sub.2--CO--O--Ph-- CuBr/Me.sub.6-TREN 260:1:4:4 20
750 - 1.80 2 90 oDCB Ph--O--CO--C(CH.sub.3).sub.2--Br 39
Cl--(CN)CHCH.sub.3 CuC.dbd.C--Ph/bpy 100:1:1.5:3 19 1,300 3.60 15
90 DM- F 40 Cl--(CN)CHCH.sub.3 CuSPh/bpy 140:1:0.7:1.2 19 2,800
3.30 13 60 DMF 41 I--CH(Cl)--CH.sub.3 CuBr/Me.sub.6-TREN 260:1:2:4
44 3,200 1.30 5 90 oDC- B 42 I--CH(Cl)--CH.sub.3 CuBr/Me.sub.6-TREN
520:1:4:4 20 4,100 1.27 3 130 oD- CB 43 I--CH(Cl)--CH.sub.3
CuBr/Me.sub.6-TREN 60:1:1:1 20 2,000 1.40 3 90 oDCB 44
I--CH(Cl)--CH.sub.3 Cul/Me.sub.6-TREN 130:1:1:1 20 1,700 1.21 2 90
oDCB- 45 I--CH.sub.2--Ph--CH.sub.2--I CuBr/Me.sub.6-TREN 520:1:8:8
20 4,400 1.50- 4 130 oDCB 46 NCS--CH.sub.2--Ph--CH.sub.2--SCN
Cu.sub.2Te/bpy 260:1:4:8 22 5,100 2.23- 8 130 oDCB 47
NCS--CH.sub.2--Ph--CH.sub.2--SCN CuBr/Me.sub.6-TREN 520:1:4:4 20
1,000 - 1.55 2 130 oDCB .sup.a)Molar ratio of VC to initiator to
catalyst to ligand.
TABLE-US-00004 TABLE 4 Polymerization of Vinyl Chloride Initiated
from Various Halides and Catalyzed by Cu (0). Conv, M.sub.w/ Temp
Exp Initiator Catalyst/Ligand [VC]:[I]:[C]:[L].sup.a) Time, h % Mn
M.sub.n .degree. C. Solvent 48
Cl--CH.sub.2--C(CH.sub.2--Cl).dbd.CH.sub.2 Cu(0)/bpy 200:1:4:8 20
31 7,- 700 1.85 130 oDCB 49 Cl--CH.sub.2--CH.dbd.C(CH.sub.3).sub.2
Cu(0)/bpy 100:1:2:4 20 20 8,300 - 1.62 130 oDCB 50
Cl--CH.sub.2--CH.dbd.CH.sub.2 Cu(0)/bpy 100:1:2:4 20 27 6,100 1.83
130 - oDCB 51 Cl--CH(CN)CH.sub.3 Cu(0)/bpy 130:1:1.2:1.2 19 20
6.900 1.85 90 DMF 52 Cl--CH(CN)CH.sub.3 Cu(0)/bpy 130:1:1.2:2.4 19
12 7,300 1.93 130 oDCB 53 Cl--CH.sub.2--Cl Cu(0)/bpy 100:1:2:4 20 5
50,000 2.75 130 oDCB 54 Cl--CH.sub.2--Ph--CH.sub.2--Cl Cu(0)/bpy
260:1:4:8 21 34 5,600 1.62 130- oDCB 55
Cl--CH.sub.2--Ph--CH.sub.2--Cl Cu(0)/bpy 1000:1:8:16 20 18 22,400
1.53 - 130 oDCB 56 Cl--CH.sub.2--Ph--CH.sub.2--Cl Cu(0)/bpy
60:1:4:4 20 95 gel -- 130 oDCB- 57 Br--(CH.sub.3).sub.2C--COBr
Cu(0)/bpy 130:1:4:8 22 12 17,000 1.90 90 oD- CB 58
Br--(CH.sub.3).sub.2C--COOEt Cu(0)/bpy 130:1:1.2:1.8 22 20 8,100
1.85 9- 0 oDCB 59 Br--(CH.sub.3).sub.2C--COOEt
Cu(0)/bpy/Al.sup.iBu.sub.3 130:1:1.2:1.8:1- .2 22 77 6,400 1.85 90
oDCB 60 (Br--CH.sub.2).sub.4Ph Cu(0)/bpy 125:1:8:16 20 7 23,700
1.58 130 oDCB 61
Br--C(CH.sub.3).sub.2--COO--Ph--C(CH.sub.3).sub.2-- Cu(0)/bpy
260:1:4:8- 17 30 6,300 1.45 130 oDCB Ph--OCO--C(CH.sub.3).sub.2--Br
62 Br--C(CH.sub.3).sub.2--COO--Ph--C(CH.sub.3).sub.2-- Cu(0)/bpy
260:1:4:8- 65 42 11,100 1.72 90 oDCB Ph--OCO--C(CH.sub.3).sub.2--Br
63 Br--C(CH.sub.3).sub.2--COO--Ph--C(CH.sub.3).sub.2--
Cu(0)/bpy/Nal 260:1- :3:4.5:3 20 20 4,200 1.50 130 oDCB
Ph--OCO--C(CH.sub.3).sub.2--Br 64
Br--C(CH.sub.3).sub.2--CO--O--Ph-- Cu(0)/PMDETA 260:1:4:8 20 35 gel
-- - 90 oDCB Ph--O--CO--C(CH.sub.3).sub.2--Br 65
Br--C(CH.sub.3).sub.2--CO--O--Ph-- Cu(0)/bpy 260:1:4:8 22 30 5,700
1.48- 130 oDCB Ph--OCO--C(CH.sub.3).sub.2--Br 66
Br--C(CH.sub.3).sub.2--OCO--Ph--C(CH.sub.3)-- Cu(0)/bpy 390:1:6:12
18 1- 4 6,800 1.98 130 oDCB [(Ph--OCO--C(CH.sub.3).sub.2--Br].sub.2
67 Br--CH(Cl)--CH.sub.3 Cu(0)/bpy 100:1:2:4 20 40 6,000 2.30 130
oDCB 68 Br--CH(Ph)CH.sub.3 Cu(0)/bpy 130:1:2.2:3 66 26 6,000 1.75
130 oDCB 69 Br--CH(Ph)CH.sub.3 Cu(0)/bpy/Nal 130:1:2:4:2 24 26
4,300 1.70 130 oDCB 70 Br--CH.sub.2--Ph--CH.sub.2--Br Cu(0)/bpy
260:1:4:8 20 43 11,000 1.63 13- 0 oDCB 71
Br--N(CO--CH.sub.2--CH.sub.2--CO) Cu(0)/bpy 130:1:2:4 20 1 5,600
1.60 1- 30 oDCB 72 I--C(CH.sub.3).sub.2--CO--O--Ph-- Cu(0)/bpy
260:1:4:8 20 38 6,700 1.47 - 130 oDCB
Ph--O--CO--C(CH.sub.3).sub.2--I 73
I--C(CH.sub.3).sub.2--CO--O--Ph--C(CH.sub.3).sub.2-- Cu(0)/bpy
260:1:4:- 8 21 28 7,000 1.60 90 oDCB
Ph--O--CO--C(CH.sub.3).sub.2--I 74
I--C(CH.sub.3).sub.2--OC--OPh--C(CH.sub.3)-- Cu(0)/bpy 390:1:6:12
70 30- 8,600 1.67 130 oDCB [(Ph--OCO--C(CH.sub.3).sub.2--I].sub.2
75 I--CF.sub.2--(CF.sub.2).sub.8--CF.sub.3 Cu(0)/bpy 130:1:2:4 22
26 5,800- 1.64 130 oDCB 76 I--CH.sub.2--CH.dbd.CH.sub.2 Cu(0)/bpy
130:1:1.2:2.2 20 13.5 6,500 1.70- 90 oDCB 77
I--CH.sub.2--CH.dbd.CH.sub.2 Cu(0)/bpy 130:1:5:2.5 22 27 13,100
1.93 90- oDCB 78 I--CH.sub.2--CH.dbd.CH.sub.2 Cu(0)/bpy 260:1:2:4
24 22 6,800 1.72 130 o- DCB 79 I--CH.sub.2--CH.dbd.CH.sub.2
Cu(0)/bpy 260:1:2:2 20 12 3,400 1.84 130 o- DCB 80 CHI.sub.3
Cu(0)/bpy 50:1:1.5:3 20 8 3,300 1.25 130 oDCB 81 CHI.sub.3
Cu(0)/bpy 50:1:3:6 20 40 3,700 1.65 130 oDCB 82 CHI.sub.3 Cu(0)/bpy
150:1:3:6 20 19 4,500 1.35 130 oDCB 83 CHI.sub.3 Cu(0)/bpy
150:1:1.5:3 20 3 760 1.38 130 oDCB 84 CHI.sub.3 Cu(0)/bpy
150:1:6:12 20 33 6,100 1.65 130 oDCB 85 CHI.sub.3 Cu(0)/bpy
1500:1:6:12 20 7 17,400 1.40 130 oDCB 86 CHI.sub.3 Cu(0)/bpy
1500:1:12:24 20 11 30,000 1.63 130 oDCB 87 CHI.sub.3 Cu(0)/bpy
1500:1:12:24 20 1 11,400 1.55 90 oDCB 88 CHI.sub.3 Cu(0)/bpy
3100:1:12:24 20 8 45,000 1.59 130 oDCB 89 CHI.sub.3 Cu(0)/TREN
150:1:0.75:0.75 20 10 5,000 1.58 130 oDCB 90 Cl.sub.4 Cu(0)/bpy
150:1:4:8 20 2 2,500 1.45 130 oDCB 91 Cl.sub.4 Cu(0)/bpy
1000:1:8:16 20 7 17,400 1.52 130 oDCB 92 I--CH(Cl)--CH.sub.3
Cu(0)/bpy 130:1:2:4 67 28 3,500 1.75 130 oDCB 93
I--CH(Cl)--CH.sub.3 Cu(0)/bpy 130:1:2:4 21 42 3,900 1.65 90 oDCB 94
I--CH(Cl)--CH.sub.3 Cu(0)/bpy 130:1:2:4 44 36 8,400 1.55 60 oDCB 95
I--CH(Cl)--CH.sub.3 Cu(0)/bpy 520:1:2:4 44 13 7,700 1.70 90 oDCB 96
I--CH(Cl)--CH.sub.3 Cu(0)/TREN 520:1:1:1 20 28 7,900 1.65 130 oDCB
97 I--CH(Cl)--CH.sub.3 Cu(0)/bpy 100:1:2:4 20 15 5,200 1.78 60 Bulk
98 I--CH(Cl)--CH.sub.3 Cu(0)/bpy 100:1:2:4 20 22 5,600 1.77 60
o-DCB 99 I--CH(Cl)--CH.sub.3 Cu(0)/bpy 100:1:2:4 20 26 6,200 1.78
60 o-DCB 100 I--CH(Cl)--CH.sub.3 Cu(0)/bpy 100:1:2:4 20 14 6.500
1.69 60 o-DCB 101 I--CH(Cl)--CH.sub.3 Cu(0)/bpy 100:1:2:4 20 18
5,400 1.87 90 Bulk 102 I--CH(Cl)--CH.sub.3 Cu(0)/bpy 100:1:2:4 20
45 7,800 1.67 90 o-DCB 103 I--CH(Cl)--CH.sub.3 Cu(0)/bpy 100:1:2:4
20 55 7,300 1.79 90 o-DCB 104 I--CH(Cl)--CH.sub.3 Cu(0)/bpy
100:1:2:4 20 52 8,300 1.68 90 o-DCB 105 I--CH(Cl)--CH.sub.3
Cu(0)/bpy 100:1:2:4 20 39 5,500 1.78 130 o-DCB 106
I--CH(Cl)--CH.sub.3 Cu(0)/bpy 100:1:2:4 20 38 6,100 1.77 130 o-DCB
107 I--CH(Cl)--CH.sub.3 Cu(0)/bpy 100:1:2:4 20 43 7,100 1.65 130
o-DCB 108 I--CH(Cl)--CH.sub.3 Cu(0)/bpy 100:1:2:4 20 39 6,800 1.68
130 o-DCB 109 I--CH(Cl)--CH.sub.3 Cu(0)/bpy/NaDDS 100:1:2:4:0.1 20
53 10,600 1.65 90- H.sub.2O 110 I--CH(Cl)--CH.sub.3 Cu(0)/bpy/NaDDS
100:1:2:4:0.5 20 47 8,500 1.69 90 - H.sub.2O 111
I--CH(Cl)--CH.sub.3 Cu(0)/bpy/NaDDS 100:1:2:4:1 20 41 7,000 1.75 90
H.- sub.2O 112 I--CH(Cl)--CH.sub.3 Cu(0)/bpy/NaDDS 100:1:2:4:2 20
43 7,500 1.66 90 H.- sub.2O 113 I--CH(Cl)--CH.sub.3 Cu(0)/bpy/NaDDS
100:1:2:4:4 20 45 7,300 1.72 90 H.- sub.2O 114 I--CH(Cl)--CH.sub.3
Cu(0)/bpy/NaDDS 100:1:2:4:0.5 1 30 4,700 1.67 90 H- .sub.2O 115
I--CH(Cl)--CH.sub.3 Cu(0)/bpy/NaDDS 100:1:2:4:0.5 2 34 6,200 1.71
90 H- .sub.2O 116 I--CH(Cl)--CH.sub.3 Cu(0)/bpy/NaDDS 100:1:2:4:0.5
4 44 7,100 1.76 90 H- .sub.2O 117 I--CH(Cl)--CH.sub.3
Cu(0)/bpy/NaDDS 100:1:2:4:0.5 8 49 8,500 1.72 90 H- .sub.2O 118
I--CH.sub.2--Ph--CH.sub.2--I Cu(0)/bpy 80:1:4:8 20 35 7,900 1.61
130 o- DCB 119 I--CH.sub.2--Ph--CH.sub.2--I Cu(0)/bpy 130:1:4:8 20
31 10,300 1.58 130- oDCB 120 I--CH.sub.2--Ph--CH.sub.2--I Cu(0)/bpy
260:1:4:8 20 19 8,400 1.55 130 - Et.sub.2CO.sub.3 121
I--CH.sub.2--Ph--CH.sub.2--I Cu(0)/Me.sub.6-TREN 260:1:4:4 20 14
3,000- 1.80 130 oDCB 122 I--CH.sub.2--Ph--CH.sub.2--I Cu(0)/TREN
520:1:4:4 20 37 Gel -- 130 oDC- B 123 I--CH.sub.2--Ph--CH.sub.2--I
Cu(0)/bpy 520:1:4:8 20 5 3,100 2.05 130 D- MSO 124
I--CH.sub.2--Ph--CH.sub.2--I Cu(0)/bpy 130:1:2:4 22 18 6,100 2.02
130 - DMF 125 I--CH.sub.2--Ph--CH.sub.2--I Cu(0)/bpy 260:1:4:8 1
1.5 1,100 1.98 130 - oDCB 126 I--CH.sub.2--Ph--CH.sub.2--I
Cu(0)/bpy 260:1:4:8 2 6.6 4,100 1.65 130 - oDCB 127
I--CH.sub.2--Ph--CH.sub.2--I Cu(0)/bpy 260:1:4:8 4 11 7,600 1.48
130 o- DCB 128 I--CH.sub.2--Ph--CH.sub.2--I Cu(0)/bpy 260:1:4:8 7
13.4 8,300 1.46 130- oDCB 129 I--CH.sub.2--Ph--CH.sub.2--I
Cu(0)/bpy 260:1:4:8 13 17.5 10,400 1.48 1- 30 oDCB 130
I--CH.sub.2--Ph--CH.sub.2--I Cu(0)/bpy 520:1:4:8 2 2.2 2,100 2.10
130 - oDCB 131 I--CH.sub.2--Ph--CH.sub.2--I Cu(0)/bpy 520:1:4:8 5
7.5 7,019 1.49 130 - oDCB 132 I--CH.sub.2--Ph--CH.sub.2--I
Cu(0)/bpy 520:1:4:8 11 11 11,000 1.45 130- oDCB 133
I--CH.sub.2--Ph--CH.sub.2--I Cu(0)/bpy/Al.sup.iBu.sub.3
520:1:4:8:2.6 - 22 20 12,700 1.59 130 oDCB 134
I--CH.sub.2--Ph--CH.sub.2--I Cu(0)/bpy 520:1:8:8 21 20 29,600 1.89
130- oDCB 135 I--CH.sub.2--Ph--CH.sub.2--I Cu(0)/bpy 520:1:16:8 21
43 gel -- 130 oDC- B 136 I--CH.sub.2--Ph--CH.sub.2--I
Cu(0)/bpy/DtBP 1000:1:4:8:8 20 16 14,200 - 1.49 130 oDCB 137
I--CH.sub.2--Ph--CH.sub.2--I Cu(0)/bpy 1000:1:16:32 20 17 16,400
1.63 - 130 oDCB 138 I--CH.sub.2--Ph--CH.sub.2--I Cu(0)/bpy
1000:1:8:16 20 9 15,500 1.59 13- 0 oDCB 137
I--CH.sub.2--Ph--CH.sub.2--I Cu(0)/bpy 260:1:4:8 23 20 21,000 1.60
130- oDCB 139 NCS--CH.sub.2--Ph--CH.sub.2--SCN Cu(0)/bpy 260:1:4:8
20 26 11,000 3.14- 130 oDCB .sup.a)Molar ratio of VC to initiator
to catalyst to ligand.
TABLE-US-00005 TABLE 5 Polymerization of Vinyl Chloride catalyzed
by Various Metal Derivatives and Metals in their Zero Oxidation
State. Temp Exp Initiator Catalyst/Ligand [VC]:[I]:[C]:[L].sup.a)
Time, h Mn Conv % M.sub.w/M.sub.n .degree. C. Solvent 140
Br--(CH.sub.3).sub.2C--COOEt Al(0)/bpy 130:1:1.3:1.1 17 8,200 5
1.61 9- 0 xylene 141 Br--(CH.sub.3).sub.2C--COOEt Al.sup.iBu.sub.3
130:1:1.14 19 12,800 30 - 1.68 90 oDCB 142
Br--(CH.sub.3).sub.2C--COOEt Cd(0)/bpy 130:1:1.2:1.1 22 14,000 14
1.65- 90 oDCB 143 Br--(CH.sub.3).sub.2C--COOEt Sm(0)/bpy
130:1:1.2:1.4 19 11,400 11 1.64- 90 dioxane 144
Br--(CH.sub.3).sub.2C--COOEt Zn(0)/bpy 130:1:1.2:1.6 20 14,400 15
1.68- 90 oDCB 145 Cl--CH(CN)--CH.sub.3 Cr(CO).sub.6 130:1:1.2 18
18,400 9 1.57 90 oDCB .sup.a)Molar ratio of VC to initiator to
catalyst to ligand.
TABLE-US-00006 TABLE 6 Selected Examples of the Room Temperature
Polymerization of Vinyl Chloride Catalyzed by Copper Catalysts in
Water, Solvents and Mixtures Thereof. [VC]/[I]/ Mw/ Time Exp
Initiator Catalyst [C]/[L]/[S].sup.a) Mn Mn h Conv. % Temp .degree.
C. Solvent 146 CH.sub.3--CH(Cl)--I Cu(0)/NH.sub.4OH 100/1/1/2 8,200
1.75 48 30 20 NH.- sub.4OH 147 CH.sub.3--CH(Cl)--I Cu(0)/TREN
100/1/2/4 13,500 1.60 20 67 20 o-DCB 148 CH.sub.3--CH(Cl)--I
Cu(0)/TREN 100/1/2/4 5,500 1.61 20 45 20 H.sub.2O 149
CH.sub.3--CH(Cl)--I Cu(0)/TREN 100/1/2/4 3,700 1.47 20 11 20 THF
150 CH.sub.3--CH(Cl)--I Cu(0)/TREN 100/1/2/4 4,700 1.57 16 26 20
DMF 151 CH.sub.3--CH(Cl)--I Cu(0)/TREN 100/1/2/2 11,500 1.60 20 75
20 o-DCB 152 CH.sub.3--CH(Cl)--I Cu(0)/TREN 100/1/1/2 7,000 1.65 20
65 20 o-DCB 153 CH.sub.3--CH(Cl)--I Cu(0)/TREN/Brij-97
100/1/2/4/0.5 5,500 1.91 20 54 - 20 H.sub.2O 154
CH.sub.3--CH(Cl)--I Cu(0)/TREN/NaDDS 100/1/2/4/0.5 13,200 1.54 20
95 2- 0 H.sub.2O 155 CH.sub.3--CH(Cl)--I Cu(0)/TREN/NaDDS
100/1/2/4/0.5 2,600 1.91 1 8 20 H- .sub.2O 156 CH.sub.3--CH(Cl)--I
Cu(0)/TREN/NaDDS 100/1/2/4/0.5 4,350 1.65 2 27 20 - H.sub.2O 157
CH.sub.3--CH(Cl)--I Cu(0)/TREN/NaDDS 100/1/2/4/0.5 6,440 1.56 4 55
20 - H.sub.2O 158 CH.sub.3--CH(Cl)--I Cu(0)/TREN/NaDDS
100/1/2/4/0.5 8,300 1.47 8 62 20 - H.sub.2O 159 CH.sub.3--CH(Cl)--I
Cu(0)/TREN/NaDDS 500/1/2/4/0.5 24,000 1.60 48 51 2- 0 H.sub.2O 160
CH.sub.3--CH(Cl)--I Cu.sub.2O/TREN/NaDDS 100/1/2/4/0.5 12,500 2.43
20 - 81 25 H.sub.2O 161 CH.sub.3--CH(Cl)--I Cu.sub.2S/TREN/NaDDS
100/1/2/4/0.5 3,700 1.57 20 4- 0 25 H.sub.2O 162
CH.sub.3--CH(Cl)--I Cu.sub.2Se/TREN/NaDDS 100/1/2/4/0.5 6,800 1.56
20 - 84 25 H.sub.2O 163 CH.sub.3--CH(Cl)--I Cu.sub.2Te/Cu(0)/
100/1/1/1/4/0.5 2,900 2.01 15 35- 25 H.sub.2O TREN/NaDDS 164
CH.sub.3--CH(Cl)--I Cu.sub.2Te/TREN/ 100/1/2/4 5,500 1.81 15 44 25
H.s- ub.2O 165 CH.sub.3--CH(Cl)--I Cu.sub.2Te/TREN/Brij97
100/1/2/4/0.5 6,500 1.72 17- 88 25 H.sub.2O 166 CH.sub.3--CH(Cl)--I
Cu.sub.2Te/TREN/Brij98 100/1/2/4/0.5 8,600 1.75 17- 98 25 H.sub.2O
167 CH.sub.3--CH(Cl)--I Cu.sub.2Te/TREN/NaDDS 100/1/2/4/2.5 6,700
2.10 17 - 92 25 H.sub.2O 168 CH.sub.3--CH(Cl)--I
Cu.sub.2Te/TREN/NaDDS 100/1/2/4/1 8,100 1.68 17 96- 25 H.sub.2O 169
CH.sub.3--CH(Cl)--I Cu.sub.2Te/TREN/NaDDS 100/1/2/4/0.5 8,600 1.58
20 - 96 25 H.sub.2O 170 CH.sub.3--CH(Cl)--I Cu.sub.2Te/TREN/NaDDS
100/1/2/4/0.5 7,900 2.14 14 - 93 25 H.sub.2O 171
CH.sub.3--CH(Cl)--I Cu.sub.2Te/TREN/NaDDS 100/1/1/2/0.5 5,900 1.75
17 - 76 25 H.sub.2O 172 CH.sub.3--CH(Cl)--I Cu.sub.2Te/TREN/NaDDS
100/1/2/4/0.1 5,500 1.76 17 - 69 25 H.sub.2O 173
CH.sub.3--CH(Cl)--I CuBr/TREN/Brij 98 100/1/0.5/1/0.5 4,100 1.88 16
31 25 H.sub.2O 174 CH.sub.3--CH(Cl)--I CuCl/TREN/Brij 98
100/1/1/1.5/0.5 8,500 1.86 48 73 20 H.sub.2O 175
CH.sub.3--CH(Cl)--I CuCl/TREN/Brij-97 100/1/2/4/0.5 19,700 2.02 20
84 - 20 H.sub.2O 176 CH.sub.3--CH(Cl)--I CuCl/TREN/NaDDS
100/1/2/4/0.5 15,500 2.20 20 67 20- H.sub.2O 177
CH.sub.3--CH(Cl)--I Cul/TREN/Brij-97 100/1/2/4/0.5 20,800 1.97 20
13 2- 0 H.sub.2O 178 CH.sub.3--CH(Cl)--I CuSPh/TREN/NaDDS 100/1/2/4
5500 1.80 18 60 25 H.su- b.2O 179 CHI.sub.3 Cu(0)/PMDETA/NaDDS
100/1/2/4 3500 1.59 21 18 25 H.sub.2O 180 CHI.sub.3 Cu(0)/TREN/
100/1/2/4 8330 5.32 87 70 25 MeOH 181 CHI.sub.3 Cu(0)/TREN/
100/1/2/4/0.5 1,000 1.47 13 5 25 H.sub.2O
(CH.sub.3).sub.3NC.sub.16H.sub.33Cl 182 CHI.sub.3 Cu(0)/TREN/NaDDS
1000/1/100/100/5 25,000 2.20 16 23 25 H.sub- .2O 183 CHI.sub.3
Cu(0)/TREN/NaDDS 1000/1/100/100/5 36,000 3.66 87 65 25 H.sub- .2O
184 CHI.sub.3 Cu(0)/TREN/NaDDS 800/1/30/30/4 43,000 2.29 66 90 25
H.sub.2O- 185 CHI.sub.3 Cu(0)/TREN/NaDDS 800/1/15/15/4 33,500 2.44
66 60 25 H.sub.2O- 186 CHI.sub.3 Cu(0)/TREN/NaDDS 200/1/4/8/2
14,900 1.63 20 63 20 H.sub.2O 187 CHI.sub.3 Cu(0)/TREN/NaDDS
100/1/8/8/0.5 10,600 1.57 13 94 25 H.sub.2O- 188 CHI.sub.3
Cu(0)/TREN/NaDDS 300/1/6/9/1.5 5,800 1.77 16 19 25 MeOH 189
CHI.sub.3 Cu(0)/TREN/NaDDS 100/1/4/4/0.5 8,400 1.72 17 88 25
H.sub.2O 190 CHI.sub.3 Cu(0)/TREN/NaDDS 100/1/2/4/0.5 1,300 1.22 17
8 25 MeOH 191 CHI.sub.3 Cu(0)/TREN/NaDDS 100/1/2/4/0.5 1100 1.55 1
10 25 H.sub.2O 192 CHI.sub.3 Cu(0)/TREN/NaDDS 100/1/2/4/0.5 1358
1.58 2 20 25 H.sub.2O 193 CHI.sub.3 Cu(0)/TREN/NaDDS 100/1/2/4/0.5
1728 1.58 4 25 25 H.sub.2O 194 CHI.sub.3 Cu(0)/TREN/NaDDS
100/1/2/4/0.5 1,970 1.56 7 28 25 H.sub.2O 195 CHI.sub.3
Cu(0)/TREN/NaDDS 100/1/2/4/0.5 2,800 1.54 14 39 25 H.sub.2O 196
CHI.sub.3 Cu(0)/TREN/NaDDS 100/1/2/4/0.5 5500 1.57 24 69 25
H.sub.2O 197 CHI.sub.3 Cu(0)/TREN/NaDDS 100/1/2/4/0.5 8400 1.81 62
99 25 H.sub.2O 198 CHI.sub.3 Cu(0)/TREN/NaDDS 100/1/2/4/0.5 7,263
1.79 37 93 25 H.sub.2O 199 CHI.sub.3 Cu(0)/TREN/NaDDS 100/1/2/4/0.5
8,100 1.83 50 99 25 H.sub.2O 200 CHI.sub.3 Cu(0)/TREN/NaDDS
100/1/2/4/0.5 9,300 1.70 16 31 25 Acetone 201 CHI.sub.3
Cu(0)/TREN/NaDDS 100/1/2/4/0.5 10,500 1.80 15 60 25 EtOAc 202
CHI.sub.3 Cu(0)/TREN/NaDDS 100/1/2/4/0.5 8293 1.80 41 99 25
H.sub.2O 203 CHI.sub.3 Cu(0)/TREN/NaDDS 100/1/2/4/0.5 7980 1.74 30
94 25 H.sub.2O 204 CHI.sub.3 Cu(0)/TREN/NaDDS 800/1/6/6/0.5 6,900
1.77 13 7 25 H.sub.2O 205 CHI.sub.3 Cu(0)/TREN/NaDDS 100/1/2/4/0.25
9,650 2.28 68 88 25 1/1 MeOH/H.sub.2O 206 CHI.sub.3
Cu(0)/TREN/NaDDS 100/1/2/4/0.25 13,000 1.91 68 96 25 1/1THF/-
H.sub.2O 207 CHI.sub.3 Cu(0)/TREN/NaDDS 100/1/2/4/0.25 11,400 1.57
15 96 25 1/1 THF/H.sub.2O 208 CHI.sub.3 Cu(0)/TREN/NaDDS
100/1/1/2/0.5 2,600 1.37 17 35 25 H.sub.2O 209 CHI.sub.3
Cu(0)/TREN/NaDDS 100/1/0.5/1/0.5 1,700 1.35 17 26 25 H.sub.2- O 210
CHI.sub.3 Cu(0)/TREN/NaDDS 100/1/0.5/1/0.5 5700 1.76 87 87 25
H.sub.2O- 211 CHI.sub.3 Cu(0)/TREN/THF 100/1/2/4/0 11,100 1.55 15
98 25 1/1THF/H.sub- .2O 212 CHI.sub.3 Cu.sub.2Te/Cu(0)/
100/1/1/1/4/0.5 5,400 1.45 15 65 25 H.sub.- 2O TREN/NaDDS 213
CHI.sub.3 Cu.sub.2Te/CuBr/TREN/ 100/1/1/1/4/0.25/ 11,200 1.58 14 99
25- THF/H.sub.2O 1/1 Brij98/NaDDS 0.25 214 CHI.sub.3
Cu.sub.2Te/TREN/NaDDS 100/1/8/8/0.5 8,200 1.75 14 99 25 H.su- b.2O
215 CHI.sub.3 Cu.sub.2Te/TREN/NaDDS 100/1/6/6/0.5 2,600 1.53 14 54
25 H.su- b.2O 216 CHI.sub.3 Cu.sub.2Te/TREN/NaDDS 100/1/4/4/0.5
8,000 1.78 14 98 25 H.su- b.2O 217 CHI.sub.3 Cu.sub.2Te/TREN/NaDDS
100/1/2/4/0.5 5,900 1.55 13 80 25 H.su- b.2O 218 CHI.sub.3
Cu.sub.2Te/TREN/NaDDS 100/1/2/4/0.3 11,600 1.53 14 99 25 THF-
/H.sub.2O 1/2 219 CHI.sub.3 Cu.sub.2Te/TREN/NaDDS 100/1/2/4/0.25
6100 1.59 14 82 25 o-DC- B/H.sub.2O 1/1 220 CHI.sub.3
Cu.sub.2Te/TREN/NaDDS 100/1/1/2/0.5 3,300 1.38 15 45 25 H.su- b.2O
221 CHI.sub.3 Cu.sub.2Te/TREN/NaDDS 100/1/1/2/0.5 1192 1.70 2 14 25
H.sub.- 2O 222 CHI.sub.3 Cu.sub.2Te/TREN/NaDDS 100/1/1/2/0.5 2585
1.57 4 38 25 H.sub.- 2O 223 CHI.sub.3 Cu.sub.2Te/TREN/NaDDS
100/1/1/2/0.5 7883 1.82 24 99 25 H.sub- .2O 224 CHI.sub.3
Cu.sub.2Te/TREN/NaDDS 100/1/0.5/1/0.5 5,000 1.45 64 66 25 H.-
sub.2O 225 CHI.sub.3 Cu.sub.2Te/TREN/NaDDS 100/1/0.1/0.5/0.5 850
1.43 64 17 25 H.- sub.2O 226 CHI.sub.3 Cu.sub.2Te/TREN/NaDDS
100/1/0.1/0.2/0.5 920 1.42 64 11 25 H.- sub.2O 227 CHI.sub.3
Cu.sub.2Te/TREN/NaDDS 100/1/0.05/0.1/0.5 670 1.30 64 2 25 H.-
sub.2O 228 CF.sub.3--(CF.sub.2).sub.9--I Cu(0)/TREN/Brij-97
100/1/2/4/0.5 5,900 1- .66 20 64 20 H.sub.2O 229
CH.sub.2.dbd.CH--CH.sub.2--I Cu(0)/bpy 100/1/2/4 12,000 1.88 20 5
20 o- -DCB 230 BrC(CH.sub.3).sub.2--COOPh-- Cu(0)/TREN/NaDDS
200/1/4/8/1 65,000 1.92 - 20 61 20 H.sub.2O
Ph--OCO--C(CH.sub.3).sub.2Br 231 CH.sub.3C[Ph--OCO--
Cu(0)/TREN/NaDDS 300/1/3/4.5 65,000 1.70 20 18 20 - H.sub.2O
C(CH.sub.3).sub.2Br].sub.3 232 Cl--CH.sub.2--Ph--CH.sub.2--Cl
CuCl/TREN/Brij 97 50/1/2/3/0.5 62,300 1.95 20 56 20 H2O 233
I--CH.sub.2--Ph--CH.sub.2--I Cu(0)/TREN/NaDDS 260/1/4/8/1.3 22,700
1.5- 5 20 13 20 H.sub.2O 234 Ph--CO--O--O--CO--Ph CuCl/TREN/Brij 97
100/1/1.5/1 53,100 1.99 20 62 20 H.sub.2O 235 PVC, Mn = 5100,
Cu(0)/TREN/NaDDS 740/1/2/4/0.5 29,800 2.62 20 52 20 H.sub.2O Mw/Mn
= 1.6 236 PVC, Cu(0)/TREN/NaDDS 1440/1/10/20 55,700 2.94 20 20 20
H.sub.2O Mn = 22,000, Mw/Mn = 2.2 .sup.a)Molar ratio of VC to
initiator to catalyst to ligand to surfactan
TABLE-US-00007 TABLE 7 Room temperature
Na.sub.2S.sub.2O.sub.4-mediated LRP of VC initiated with iodoform
in H.sub.2O/THF Catalyst/ Electron [VC]/[I]/[C]/[ES]/ Time Conv Exp
Initator Buffer Shuttle Surfactant [B]/[S].sup.a) Mn Mw/Mn (h) (%)
Sol- vent 1 CHI.sub.3 Na.sub.2S.sub.2O.sub.4/ -- -- 200/1/2/0/
1,017 2.442 7 12.27 2- /1 NaHCO.sub.3 2.2/0 H.sub.2O/THF 2
CHI.sub.3 Na.sub.2S.sub.2O.sub.4/ -- -- 200/1/2/0/ 3,106 1.505 8
16.01 2- /1 NaHCO.sub.3 2.2/0 H.sub.2O/THF 3 CHI.sub.3
Na.sub.2S.sub.2O.sub.4/ -- -- 200/1/2/0/ 3,018 1.608 13 24.54 - 2/1
NaHCO.sub.3 2.2/0 H.sub.2O/THF 4 CHI.sub.3 Na.sub.2S.sub.2O.sub.4/
-- -- 200/1/2/0/ 4,033 1.565 15 30.84 - 2/1 NaHCO.sub.3 2.2/0
H.sub.2O/THF 5 CHI.sub.3 Na.sub.2S.sub.2O.sub.4/ -- -- 200/1/2/0/
4,688 1.499 16 35.40 - 2/1 NaHCO.sub.3 2.2/0 H.sub.2O/THF 6
CHI.sub.3 Na.sub.2S.sub.2O.sub.4/ -- -- 200/1/2/0/ 4,492 1.573 18
39.54 - 2/1 NaHCO.sub.3 2.2/0 H.sub.2O/THF 7 CHI.sub.3
Na.sub.2S.sub.2O.sub.4/ -- -- 200/1/2/0/ 5,841 1.482 20 46.20 - 2/1
NaHCO.sub.3 2.2/0 H.sub.2O/THF 8 CHI.sub.3 Na.sub.2S.sub.2O.sub.4/
-- -- 200/1/2/0/ 7,590 1.476 21 50.88 - 2/1 NaHCO.sub.3 2.2/0
H.sub.2O/THF 9 CHI.sub.3 Na.sub.2S.sub.2O.sub.4/ -- -- 200/1/2/0/
7,954 1.485 22 54.15 - 2/1 NaHCO.sub.3 2.2/0 H.sub.2O/THF 10
CHI.sub.3 Na.sub.2S.sub.2O.sub.4/ -- -- 200/1/2/0/ 6,758 1.489 23
55.78- 2/1 NaHCO.sub.3 2.2/0 H.sub.2O/THF 11 CHI.sub.3
Na.sub.2S.sub.2O.sub.4/ -- -- 200/1/2/0/ 7,301 1.471 24 57.75- 2/1
NaHCO.sub.3 2.2/0 H.sub.2O/THF 12 CHI.sub.3 Na.sub.2S.sub.2O.sub.4/
-- -- 200/1/2/0/ 8,072 1.469 27 61.89- 2/1 NaHCO.sub.3 2.2/0
H.sub.2O/THF 13 CHI.sub.3 Na.sub.2S.sub.2O.sub.4/ -- -- 200/1/2/0/
8,652 1.467 30 64.89- 2/1 NaHCO.sub.3 2.2/0 H.sub.2O/THF 14
CHI.sub.3 Na.sub.2S.sub.2O.sub.4/ -- -- 200/1/2/0/ 8,195 1.465 33
66.06- 2/1 NaHCO.sub.3 2.2/0 H.sub.2O/THF 15 CHI.sub.3
Na.sub.2S.sub.2O.sub.4/ -- -- 200/1/2/0/ 8,650 1.467 38 68.60- 2/1
NaHCO.sub.3 2.2/0 H.sub.2O/THF 16 CHI.sub.3 Na.sub.2S.sub.2O.sub.4/
-- -- 200/1/2/0/ 8,920 1.474 45 73.72- 2/1 NaHCO.sub.3 2.2/0
H.sub.2O/THF 17 CHI.sub.3 Na.sub.2S.sub.2O.sub.4/ -- -- 200/1/2/0/
9,068 1.505 51 76.09- 2/1 NaHCO.sub.3 2.2/0 H.sub.2O/THF 18
CHI.sub.3 Na.sub.2S.sub.2O.sub.4/ -- -- 200/1/2/0/ 9,977 1.479 63
77.70- 2/1 NaHCO.sub.3 2.2/0 H.sub.2O/THF 19 CHI.sub.3
Na.sub.2S.sub.2O.sub.4/ -- -- 200/1/2/0/ 8,974 1.509 66 80.95- 2/1
NaHCO.sub.3 2.2/0 H.sub.2O/THF 20 CHI.sub.3 Na.sub.2S.sub.2O.sub.4/
-- -- 200/1/2/0/ 9,654 1.500 75 80.51- 2/1 NaHCO.sub.3 2.2/0
H.sub.2O/THF 21 CHI.sub.3 Na.sub.2S.sub.2O.sub.4/ -- -- 200/1/4/0/
10,167 1.578 45 79.9- 6 2/1 NaHCO.sub.3 2.2/0 H.sub.2O/THF 22
CHI.sub.3 Na.sub.2S.sub.2O.sub.4/ -- -- 200/1/2/0/ 10,348 1.474 63
77.6- 1 2/1 NaHCO.sub.3 4/0 H.sub.2O/THF 23 CHI.sub.3
Na.sub.2S.sub.2O.sub.4 -- -- 200/1/2/0/ 1,430 1.870 63 7.64 2- /1
0/0 H.sub.2O/THF 24 CHI.sub.3 Na.sub.2S.sub.2O.sub.4/ -- --
200/1/2/0/ 9,653 1.460 63 75.11- 7/3 NaHCO.sub.3 2.2/0 H.sub.2O/THF
.sup.a)Ratio [VC]/[initiator]/[catalyst]/[electron
shuttle]/[buffer]/[surfactant] mol/mol/mol/mol/mol/ppm w/w to
monomer
TABLE-US-00008 TABLE 8 Room Temperature
Na.sub.2S.sub.2O.sub.4-mediated LRP of VC Initiated with Iodoform
in H.sub.2O/THF in the presence of surfactant Brij .RTM. 98.
Catalyst/ Electron [VC]/[I]/[C]/[ES]/ Time Conv Exp Initator Buffer
Shuttle Surfactant [B]/[S].sup.a) Mn Mw/Mn (h) (%) Sol- vent 25
CHI.sub.3 Na.sub.2S.sub.2O.sub.4/ -- Brij .RTM. 98 200/1/2/0/ 7,886
1.524 24 69.07 2/1 NaHCO.sub.3 2.2/2180 H.sub.2O/THF 26 CHI.sub.3
Na.sub.2S.sub.2O.sub.4/ -- Brij .RTM. 98 200/1/2/0/ 10,006 1.479 45
79.94 2/1 NaHCO.sub.3 2.2/2180 H.sub.2O/THF 27 CHI.sub.3
Na.sub.2S.sub.2O.sub.4/ -- Brij .RTM. 98 200/1/2/0/ 2,282 2.328 7
18.18 7/3 NaHCO.sub.3 2.2/2180 H.sub.2O/THF 28 CHI.sub.3
Na.sub.2S.sub.2O.sub.4/ -- Brij .RTM. 98 200/1/2/0/ 2,312 2.428 9
18.87 7/3 NaHCO.sub.3 2.2/2180 H.sub.2O/THF 29 CHI.sub.3
Na.sub.2S.sub.2O.sub.4/ -- Brij .RTM. 98 200/1/2/0/ 3,769 1.791 14
27.24 7/3 NaHCO.sub.3 2.2/2180 H.sub.2O/THF 30 CHI.sub.3
Na.sub.2S.sub.2O.sub.4/ -- Brij .RTM. 98 200/1/2/0/ 7,120 1.508 15
56.53 7/3 NaHCO.sub.3 2.2/2180 H.sub.2O/THF 31 CHI.sub.3
Na.sub.2S.sub.2O.sub.4/ -- Brij .RTM. 98 200/1/2/0/ 4,562 1.642 15
35.19 7/3 NaHCO.sub.3 2.2/2180 H.sub.2O/THF 32 CHI.sub.3
Na.sub.2S.sub.2O.sub.4/ -- Brij .RTM. 98 200/1/2/0/ 7,165 1.523 16
52.41 7/3 NaHCO.sub.3 2.2/2180 H.sub.2O/THF 33 CHI.sub.3
Na.sub.2S.sub.2O.sub.4/ -- Brij .RTM. 98 200/1/2/0/ 8,639 1.486 16
62.08 7/3 NaHCO.sub.3 2.2/2180 H.sub.2O/THF 34 CHI.sub.3
Na.sub.2S.sub.2O.sub.4/ -- Brij .RTM. 98 200/1/2/0/ 4,453 1.579 17
34.37 7/3 NaHCO.sub.3 2.2/2180 H.sub.2O/THF 35 CHI.sub.3
Na.sub.2S.sub.2O.sub.4/ -- Brij .RTM. 98 200/1/2/0/ 9,012 1.504 17
61.66 7/3 NaHCO.sub.3 2.2/2180 H.sub.2O/THF 36 CHI.sub.3
Na.sub.2S.sub.2O.sub.4/ -- Brij .RTM. 98 200/1/2/0/ 7,174 1.514 18
54.72 7/3 NaHCO.sub.3 2.2/2180 H.sub.2O/THF 37 CHI.sub.3
Na.sub.2S.sub.2O.sub.4/ -- Brij .RTM. 98 200/1/2/0/ 4,811 1.676 20
37.04 7/3 NaHCO.sub.3 2.2/2180 H.sub.2O/THF 38 CHI.sub.3
Na.sub.2S.sub.2O.sub.4/ -- Brij .RTM. 98 200/1/2/0/ 7,460 1.492 20
57.25 7/3 NaHCO.sub.3 2.2/2180 H.sub.2O/THF 39 CHI.sub.3
Na.sub.2S.sub.2O.sub.4/ -- Brij .RTM. 98 200/1/2/0/ 7,197 1.483 21
60.54 7/3 NaHCO.sub.3 2.2/2180 H.sub.2O/THF 40 CHI.sub.3
Na.sub.2S.sub.2O.sub.4/ -- Brij .RTM. 98 200/1/2/0/ 4,057 1.849 22
32.02 7/3 NaHCO.sub.3 2.2/2180 H.sub.2O/THF 41 CHI.sub.3
Na.sub.2S.sub.2O.sub.4/ -- Brij .RTM. 98 200/1/2/0/ 8,866 1.512 22
64.50 7/3 NaHCO.sub.3 2.2/2180 H.sub.2O/THF 42 CHI.sub.3
Na.sub.2S.sub.2O.sub.4/ -- Brij .RTM. 98 200/1/2/0/ 7,606 1.505 24
66.62 7/3 NaHCO.sub.3 2.2/2180 H.sub.2O/THF 43 CHI.sub.3
Na.sub.2S.sub.2O.sub.4/ -- Brij .RTM. 98 200/1/2/0/ 8,865 1.511 28
69.50 7/3 NaHCO.sub.3 2.2/2180 H.sub.2O/THF 44 CHI.sub.3
Na.sub.2S.sub.2O.sub.4/ -- Brij .RTM. 98 200/1/2/0/ 9,325 1.487 44
72.18 7/3 NaHCO.sub.3 2.2/2180 H.sub.2O/THF 45 CHI.sub.3
Na.sub.2S.sub.2O.sub.4/ -- Brij .RTM. 98 200/1/2/0/ 9,419 1.527 48
73.66 7/3 NaHCO.sub.3 2.2/2180 H.sub.2O/THF 46 CHI.sub.3
Na.sub.2S.sub.2O.sub.4/ -- Brij .RTM. 98 200/1/2/0/ 10,793 1.510 56
79.81 7/3 NaHCO.sub.3 2.2/2180 H.sub.2O/THF 47 CHI.sub.3
Na.sub.2S.sub.2O.sub.4/ -- Brij .RTM. 98 200/1/2/0/ 10,124 1.54 66
80.33 7/3 NaHCO.sub.3 2.2/2180 H.sub.2O/THF 48 CHI.sub.3
Na.sub.2S.sub.2O.sub.4/ -- Brij .RTM. 98 200/1/2/0/ 8,892 1.551 66
78.23 2/1 NaHCO.sub.3 2.2/2180 H.sub.2O/THF 49 CHI.sub.3
Na.sub.2S.sub.2O.sub.4/ -- Brij .RTM. 98 200/1/2/0/ 10,139 1.570 24
70.58 2/1 NaHCO.sub.3 2.2/4160 H.sub.2O/THF 50 CHI.sub.3
Na.sub.2S.sub.2O.sub.4/ -- Brij .RTM. 98 200/1/2/0/ 11,106 1.503 45
79.80 2/1 NaHCO.sub.3 2.2/4160 H.sub.2O/THF 51 CHI.sub.3
Na.sub.2S.sub.2O.sub.4/ -- Brij .RTM. 98 200/1/2/0/ 10,707 1.562 48
79.15 2/1 NaHCO.sub.3 2.2/4160 H.sub.2O/THF 52 CHI.sub.3
Na.sub.2S.sub.2O.sub.4/ -- Brij .RTM. 98 200/1/2/0/ 11,076 1.562 66
79.13 2/1 NaHCO.sub.3 2.2/4160 H.sub.2O/THF 53 CHI.sub.3
Na.sub.2S.sub.2O.sub.4/ -- Brij .RTM. 98 200/1/2/0/ 11,669 1.533 66
75.43 7/3 NaHCO.sub.3 2.2/4160 H.sub.2O/THF 54 CHI.sub.3
Na.sub.2S.sub.2O.sub.4/ -- Brij .RTM. 98 200/1/2/0/ 12,331 1.546 45
80.44 2/1 NaHCO.sub.3 2.2/8320 H.sub.2O/THF 55 CHI.sub.3
Na.sub.2S.sub.2O.sub.4/ -- Brij .RTM. 98 200/1/2/0/ 11,679 1.626 45
80.03 2/1 NaHCO.sub.3 2.2/12480 H.sub.2O/THF 56 CHI.sub.3
Na.sub.2S.sub.2O.sub.4/ -- Brij .RTM. 98 200/1/2/0/ 10,629 1.618 45
81.10 7/3 NaHCO.sub.3 2.2/12480 H.sub.2O/THF 57 CHI.sub.3
Na.sub.2S.sub.2O.sub.4/ -- Brij .RTM. 98 200/1/2/0/ 10,260 1.616 66
79.68 2/1 NaHCO.sub.3 2.2/12480 H.sub.2O/THF 58 CHI.sub.3
Na.sub.2S.sub.2O.sub.4/ -- Brij .RTM. 98 200/1/2/0/ 10,425 1.664 45
85.00 2/1 NaHCO.sub.3 2.2/16640 H.sub.2O/THF .sup.a)Ratio
[VC]/[initiator]/[catalyst]/[electron
shuttle]/[buffer]/[surfactant] mol/mol/mol/mol/mol/ppm w/w to
monomer
TABLE-US-00009 TABLE 9 Room Temperature
Na.sub.2S.sub.2O.sub.4-mediated LRP of VC Initiated with Iodoform
in H.sub.2O/THF in the presence of electron shuttle OV.sup.2+ and
surfactant Brij .RTM. 98 Catalyst/ Electron [VC]/[I]/[C]/[ES]/ Time
Conv Exp Init Buffer Shuttle Surfactant [B]/[S].sup.a) Mn Mw/Mn (h)
(%) Solvent- 59 CHI.sub.3 Na.sub.2S.sub.2O.sub.4/ OV.sup.2+ Brij
.RTM. 98 200/1/2/0.00175/ 1,349 2.205 1 9.35 7/3 NaHCO.sub.3
2.2/2180 H.sub.2O/THF 60 CHI.sub.3 Na.sub.2S.sub.2O.sub.4/
OV.sup.2+ Brij .RTM. 98 200/1/2/0.00175/ 2,584 2.009 6 18.90 7/3
NaHCO.sub.3 2.2/2180 H.sub.2O/THF 61 CHI.sub.3
Na.sub.2S.sub.2O.sub.4/ OV.sup.2+ Brij .RTM. 98 200/1/2/0.00175/
3,348 1.802 7 24.17 7/3 NaHCO.sub.3 2.2/2180 H.sub.2O/THF 62
CHI.sub.3 Na.sub.2S.sub.2O.sub.4/ OV.sup.2+ Brij .RTM. 98
200/1/2/0.00175/ 4,261 1.749 9 30.13 7/3 NaHCO.sub.3 2.2/2180
H.sub.2O/THF 63 CHI.sub.3 Na.sub.2S.sub.2O.sub.4/ OV.sup.2+ Brij
.RTM. 98 200/1/2/0.00175/ 7,087 1.614 14 59.15 7/3 NaHCO.sub.3
2.2/2180 H.sub.2O/THF 64 CHI.sub.3 Na.sub.2S.sub.2O.sub.4/
OV.sup.2+ Brij .RTM. 98 200/1/2/0.00175/ 8,110 1.507 16 64.06 7/3
NaHCO.sub.3 2.2/2180 H.sub.2O/THF 65 CHI.sub.3
Na.sub.2S.sub.2O.sub.4/ OV.sup.2+ Brij .RTM. 98 200/1/2/0.00175/
9,455 1.484 18 65.42 7/3 NaHCO.sub.3 2.2/2180 H.sub.2O/THF 66
CHI.sub.3 Na.sub.2S.sub.2O.sub.4/ OV.sup.2+ Brij .RTM. 98
200/1/2/0.00175/ 9,087 1.511 20 70.12 7/3 NaHCO.sub.3 2.2/2180
H.sub.2O/THF 67 CHI.sub.3 Na.sub.2S.sub.2O.sub.4/ OV.sup.2+ Brij
.RTM. 98 200/1/2/0.00175/ 9,773 1.480 24 73.14 7/3 NaHCO.sub.3
2.2/2180 H.sub.2O/THF 68 CHI.sub.3 Na.sub.2S.sub.2O.sub.4/
OV.sup.2+ Brij .RTM. 98 200/1/2/0.00175/ 9,705 1.490 40 75.43 7/3
NaHCO.sub.3 2.2/2180 H.sub.2O/THF 69 CHI.sub.3
Na.sub.2S.sub.2O.sub.4/ OV.sup.2+ Brij .RTM. 98 200/1/2/0.00175/
9,853 1.546 48 77.12 7/3 NaHCO.sub.3 2.2/2180 H.sub.2O/THF 70
CHI.sub.3 Na.sub.2S.sub.2O.sub.4/ OV.sup.2+ Brij .RTM. 98
200/1/2/0.00175/ 10,175 1.546 66 79.20 7/3 NaHCO.sub.3 2.2/2180
H.sub.2O/THF 71 CHI.sub.3 Na.sub.2S.sub.2O.sub.4/ OV.sup.2+ Brij
.RTM. 98 200/1/2/0.00175/ 10,573 1.530 24 72.29 2/1 NaHCO.sub.3
2.2/4160 H.sub.2O/THF 72 CHI.sub.3 Na.sub.2S.sub.2O.sub.4/
OV.sup.2+ Brij .RTM. 98 200/1/2/0.0035/ 10,940 1.492 24 73.12 2/1
NaHCO.sub.3 2.2/2180 H.sub.2O/THF 73 CHI.sub.3
Na.sub.2S.sub.2O.sub.4/ OV.sup.2+ Brij .RTM. 98 200/1/2/0.0035/
10,455 1.592 66 83.22 7/3 NaHCO.sub.3 2.2/2180 H.sub.2O/THF 74
CHI.sub.3 Na.sub.2S.sub.2O.sub.4/ OV.sup.2+ Brij .RTM. 98
200/1/2/0.0035/ 11,592 1.542 24 73.59 2/1 NaHCO.sub.3 2.2/4160
H.sub.2O/THF 75 CHI.sub.3 Na.sub.2S.sub.2O.sub.4/ OV.sup.2+ Brij
.RTM. 98 200/1/2/0.0035/ 11,400 1.560 48 79.47 2/1 NaHCO.sub.3
2.2/4160 H.sub.2O/THF 76 CHI.sub.3 Na.sub.2S.sub.2O.sub.4/
OV.sup.2+ Brij .RTM. 98 200/1/2/0.0035/ 12,225 1.555 24 75.02 2/1
NaHCO.sub.3 2.2/8320 H.sub.2O/THF 77 CHI.sub.3
Na.sub.2S.sub.2O.sub.4/ OV.sup.2+ Brij .RTM. 98 200/1/2/0.2/2.2/
12,553 1.561 24 75.82 2/1 NaHCO.sub.3 4160 H.sub.2O/THF 78
CHI.sub.3 Na.sub.2S.sub.2O.sub.4/ OV.sup.2+ Brij .RTM. 98
200/1/2/2/2.2/ 8,152 1.70 3 35.61 2/1 NaHCO.sub.3 4160 H.sub.2O/THF
.sup.a)Ratio [VC]/[initiator]/[catalyst]/[electron
shuttle]/[buffer]/[surfactant] mol/mol/mol/mol/mol/ppm w/w to
monomer
TABLE-US-00010 TABLE 10 Room Temperature
Na.sub.2S.sub.2O.sub.4-mediated LRP of VC Initiated with Iodoform
in H.sub.2O/THF in the presence of electron shuttle MV.sup.2+ and
surfactant Brij .RTM. 98 Catalyst/ Electron [VC]/[I]/[C]/[ES]/ Time
Conv Exp Init Buffer Shuttle Surfactant [B]/[S].sup.a) Mn Mw/Mn (h)
(%) Solvent- 79 CHI.sub.3 Na.sub.2S.sub.2O.sub.4/ MV.sup.2+ Brij
.RTM. 98 200/1/2/0.00175/ 10,458 1.513 24 70.72 2/1 NaHCO.sub.3
2.2/2180 H.sub.2O/THF 80 CHI.sub.3 Na.sub.2S.sub.2O.sub.4/
MV.sup.2+ Brij .RTM. 98 200/1/2/0.00175/ 7,215 1.527 24 55.01 2/1
NaHCO.sub.3 2.2/2180 H.sub.2O/THF 81 CHI.sub.3
Na.sub.2S.sub.2O.sub.4/ MV.sup.2+ Brij .RTM. 98 200/1/2/0.00175/
2,476 2.027 7 17.84 7/3 NaHCO.sub.3 2.2/2180 H.sub.2O/THF 82
CHI.sub.3 Na.sub.2S.sub.2O.sub.4/ MV.sup.2+ Brij .RTM. 98
200/1/2/0.00175/ 2,480 1.874 9 19.63 7/3 NaHCO.sub.3 2.2/2180
H.sub.2O/THF 83 CHI.sub.3 Na.sub.2S.sub.2O.sub.4/ MV.sup.2+ Brij
.RTM. 98 200/1/2/0.00175/ 3,147 2.017 14 25.15 7/3 NaHCO.sub.3
2.2/2180 H.sub.2O/THF 84 CHI.sub.3 Na.sub.2S.sub.2O.sub.4/
MV.sup.2+ Brij .RTM. 98 200/1/2/0.00175/ 5,342 1.598 16 41.46 7/3
NaHCO.sub.3 2.2/2180 H.sub.2O/THF 85 CHI.sub.3
Na.sub.2S.sub.2O.sub.4/ MV.sup.2+ Brij .RTM. 98 200/1/2/0.00175/
5,473 1.526 18 42.98 7/3 NaHCO.sub.3 2.2/2180 H.sub.2O/THF 86
CHI.sub.3 Na.sub.2S.sub.2O.sub.4/ MV.sup.2+ Brij .RTM. 98
200/1/2/0.00175/ 9,611 1.482 20 74.62 7/3 NaHCO.sub.3 2.2/2180
H.sub.2O/THF 87 CHI.sub.3 Na.sub.2S.sub.2O.sub.4/ MV.sup.2+ Brij
.RTM. 98 200/1/2/0.00175/ 7,042 1.513 21 58.41 7/3 NaHCO.sub.3
2.2/2180 H.sub.2O/THF 88 CHI.sub.3 Na.sub.2S.sub.2O.sub.4/
MV.sup.2+ Brij .RTM. 98 200/1/2/0.00175/ 9,062 1.483 22 64.87 7/3
NaHCO.sub.3 2.2/2180 H.sub.2O/THF 89 CHI.sub.3
Na.sub.2S.sub.2O.sub.4/ MV.sup.2+ Brij .RTM. 98 200/1/2/0.00175/
8,150 1.498 24 67.00 7/3 NaHCO.sub.3 2.2/2180 H.sub.2O/THF 90
CHI.sub.3 Na.sub.2S.sub.2O.sub.4/ MV.sup.2+ Brij .RTM. 98
200/1/2/0.00175/ 7,763 1.488 28 64.46 7/3 NaHCO.sub.3 2.2/2180
H.sub.2O/THF 91 CHI.sub.3 Na.sub.2S.sub.2O.sub.4/ MV.sup.2+ Brij
.RTM. 98 200/1/2/0.00175/ 8,818 1.506 40 72.53 7/3 NaHCO.sub.3
2.2/2180 H.sub.2O/THF 92 CHI.sub.3 Na.sub.2S.sub.2O.sub.4/
MV.sup.2+ Brij .RTM. 98 200/1/2/0.00175/ 9,453 1.514 48 78.22 7/3
NaHCO.sub.3 2.2/2180 H.sub.2O/THF 93 CHI.sub.3
Na.sub.2S.sub.2O.sub.4/ MV.sup.2+ Brij .RTM. 98 200/1/2/0.00175/
9,241 1.502 51 72.52 7/3 NaHCO.sub.3 2.2/2180 H.sub.2O/THF 94
CHI.sub.3 Na.sub.2S.sub.2O.sub.4/ MV.sup.2+ Brij .RTM. 98
200/1/2/0.00175/ 9,767 1.499 54 76.64 7/3 NaHCO.sub.3 2.2/2180
H.sub.2O/THF 95 CHI.sub.3 Na.sub.2S.sub.2O.sub.4/ MV.sup.2+ Brij
.RTM. 98 200/1/2/0.00175/ 9,760 1.530 66 73.76 7/3 NaHCO.sub.3
2.2/2180 H.sub.2O/THF 96 CHI.sub.3 Na.sub.2S.sub.2O.sub.4/
MV.sup.2+ Brij .RTM. 98 200/1/2/0.0035/ 9,209 1.494 24 65.88 2/1
NaHCO.sub.3 2.2/2180 H.sub.2O/THF 97 CHI.sub.3
Na.sub.2S.sub.2O.sub.4/ MV.sup.2+ Brij .RTM. 98 200/1/2/0.0035/
8,924 1.488 24 70.76 2/1 NaHCO.sub.3 2.2/2180 H.sub.2O/THF 98
CHI.sub.3 Na.sub.2S.sub.2O.sub.4/ MV.sup.2+ Brij .RTM. 98
200/1/2/0.0035/ 10,448 1.556 24 71.38 2/1 NaHCO.sub.3 2.2/8320
H.sub.2O/THF 99 CHI.sub.3 Na.sub.2S.sub.2O.sub.4/ MV.sup.2+ Brij
.RTM. 98 200/1/2/0.0035/ 9,763 1.549 24 69.90 2/1 NaHCO.sub.3
2.2/4160 H.sub.2O/THF 100 CHI.sub.3 Na.sub.2S.sub.2O.sub.4/
MV.sup.2+ Brij .RTM. 98 200/1/2/0.007/ 10,174 1.516 24 75.90 2/1
NaHCO.sub.3 2.2/2180 H.sub.2O/THF 101 CHI.sub.3
Na.sub.2S.sub.2O.sub.4/ MV.sup.2+ Brij .RTM. 98 200/1/2/0.013/
4,984 1.729 24 36.19 2/1 NaHCO.sub.3 2.2/2180 H.sub.2O/THF
.sup.a)Ratio [VC]/[initiator]/[catalyst]/[electron
shuttle]/[buffer]/[surfactant] mol/mol/mol/mol/mol/ppm w/w to
monomer
TABLE-US-00011 TABLE 11 Room temperature
Na.sub.2S.sub.2O.sub.8--HCOONa-mediated radical polymerization of
VC initiated with bromoform in H.sub.2O/THF Catalyst/ Electron
[VC]/[I]/[C]/[ES]/ Time Conv Exp Init Buffer Shuttle Surfactant
[B]/[S].sup.a) Mn Mw/Mn (h) (%) Solvent- 102 CHBr.sub.3
Na.sub.2S.sub.2O.sub.8/ -- -- 200/1/2/2/0/ 9,539 1.941 24 7- .15
2/1 HCOONa/ -- -- 2.2/0 H.sub.2O/THF NaHCO.sub.3 103 CHBr.sub.3
Na.sub.2S.sub.2O.sub.8/ -- -- 200/1/2/2/0/ 9,042 1.943 48 2- 0.84
2/1 HCOONa/ 2.2/0 H.sub.2O/THF NaHCO.sub.3 104 CHBr.sub.3
Na.sub.2S.sub.2O.sub.8/ -- -- 200/1/2/2/0/ 8,738 1.931 72 3- 5.17
2/1 HCOONa/ 2.2/0 H.sub.2O/THF NaHCO.sub.3 105 CHBr.sub.3
Na.sub.2S.sub.2O.sub.8/ -- -- 200/1/2/2/0/ 8,157 2.018 96 4- 8.68
2/1 HCOONa/ 2.2/0 H.sub.2O/THF NaHCO.sub.3 106 CHBr.sub.3
Na.sub.2S.sub.2O.sub.8/ -- -- 200/1/2/2/0/ 8,593 1.968 120 - 53.74
2/1 HCOONa/ 2.2/0 H.sub.2O/THF NaHCO.sub.3 .sup.a)Ratio
[VC]/[initiator]/[catalyst]/[electron
shuttle]/[buffer]/[surfactant] mol/mol/mol/mol/mol/ppm w/w to
monomer
TABLE-US-00012 TABLE 12 Room temperature
Na.sub.2S.sub.2O.sub.8--HCOONa-mediated radical polymerization of
VC initiated with chloroform in H.sub.2O/THF Catalyst/ Electron
[VC]/[I]/[C]/[ES]/ Time Conv Exp Init Buffer Shuttle Surfactant
[B]/[S].sup.a) Mn Mw/Mn (h) (%) Solvent- 107 CHCl.sub.3
Na.sub.2S.sub.2O.sub.8/ -- -- 200/1/2/2/0/ 10,207 1.893 24 - 7.77
2/1 HCOONa/ -- -- 2.2/0 H.sub.2O/THF NaHCO.sub.3 108 CHCl.sub.3
Na.sub.2S.sub.2O.sub.8/ -- -- 200/1/2/2/0/ 9,535 1.906 48 2- 3.01
2/1 HCOONa/ 2.2/0 H.sub.2O/THF NaHCO.sub.3 109 CHCl.sub.3
Na.sub.2S.sub.2O.sub.8/ -- -- 200/1/2/2/0/ 8,863 1.929 72 3- 9.28
2/1 HCOONa/ 2.2/0 H.sub.2O/THF NaHCO.sub.3 110 CHCl.sub.3
Na.sub.2S.sub.2O.sub.8/ -- -- 200/1/2/2/0/ 8,854 2.154 96 5- 8.15
2/1 HCOONa/ 2.2/0 H.sub.2O/THF NaHCO.sub.3 111 CHCl.sub.3
Na.sub.2S.sub.2O.sub.8/ -- -- 200/1/2/2/0/ 7,909 1.907 120 - 56.08
2/1 HCOONa/ 2.2/0 H.sub.2O/THF NaHCO.sub.3 .sup.a)Ratio
[VC]/[initiator]/[catalyst]/[electron
shuttle]/[buffer]/[surfactant] mol/mol/mol/mol/mol/ppm w/w to
monomer
TABLE-US-00013 TABLE 13 Room temperature
H.sub.2NC(.dbd.NH)SO.sub.2H-mediated LRP of VC initiated with
iodoform in H.sub.2O/THF in the presence of electron shuttle
OV.sup.2+ Catalyst/ Electron [VC]/[I]/[C]/[ES]/ Time Conv Exp Init
Buffer Shuttle Surfactant [B]/[S] Mn Mw/Mn (h) (%) Solvent 112
CHI.sub.3 H.sub.2NC(.dbd.NH)SO.sub.2H/ OV.sup.2+ -- 200/1/2/0.0035/
1,- 352 1.933 8 10.32 7/3 NaHCO.sub.3 4.4/0 H.sub.2O/THF 113
CHI.sub.3 H.sub.2NC(.dbd.NH)SO.sub.2H/ OV.sup.2+ -- 200/1/2/0.0035/
3,- 535 1.748 16 28.14 7/3 NaHCO.sub.3 4.4/0 H.sub.2O/THF 114
CHI.sub.3 H.sub.2NC(.dbd.NH)SO.sub.2H/ OV.sup.2+ -- 200/1/2/0.0035/
5,- 662 1.563 24 45.87 7/3 NaHCO.sub.3 4.4/0 H.sub.2O/THF 115
CHI.sub.3 H.sub.2NC(.dbd.NH)SO.sub.2H/ OV.sup.2+ -- 200/1/2/0.0035/
6,- 240 1.560 48 49.68 7/3 NaHCO.sub.3 4.4/0 H.sub.2O/THF 116
CHI.sub.3 H.sub.2NC(.dbd.NH)SO.sub.2H/ OV.sup.2+ -- 200/1/2/0.0035/
7,- 119 1.489 68 54.86 7/3 NaHCO.sub.3 4.4/0 H.sub.2O/THF 117
CHI.sub.3 H.sub.2NC(.dbd.NH)SO.sub.2H/ OV.sup.2+ -- 200/1/2/0.0035/
6,- 663 1.533 96 55.53 7/3 NaHCO.sub.3 4.4/0 H.sub.2O/THF
.sup.a)Ratio [VC]/[initiator]/[catalyst]/[electron
shuttle]/[buffer]/[surfactant] mol/mol/mol/mol/mol/ppm w/w to
monomer
TABLE-US-00014 TABLE 14 Selected examples of the room temperature
non-metallic SET reagents- mediated LRP of VC in H.sub.2O, THF and
mixtures thereof Catalyst/Additive/ Electron [VC]/[I]/[C]/[A]/ES]/[
Time Conv Exp Init Buffer Shuttle Surfactant [B]/[S].sup.a) Mn
Mw/Mn (h) (%) Solvent- 118 CHI.sub.3 Na.sub.2S.sub.2O.sub.4/ --
Brij .RTM. 98 200/1/2/8/0/ 7,914 1.451 66 60.22 7/3 NaI/ 2.2/2180
H.sub.2O/THF NaHCO.sub.3 119 CHI.sub.3 Na.sub.2S.sub.2O.sub.4/
OV.sup.2+ -- 200/1/2/0/0.00175/ 10,3- 55 1.482 24 69.42 2/1
NaHCO.sub.3 2.2/0 H.sub.2O/THF 120 CHI.sub.3
Na.sub.2S.sub.2O.sub.4/ OV.sup.2+ -- 200/1/2/0/0.0035/ 9,679- 1.472
24 63.99 2/1 NaHCO.sub.3 2.2/0 H.sub.2O/THF 121 CHI.sub.3
Na.sub.2S.sub.2O.sub.4/ OV.sup.2+ -- 200/1/2/0/0.0035/ 9,020- 1.480
24 65.51 7/3 NaHCO.sub.3 2.2/0 H.sub.2O/THF 122 CHI.sub.3
Na.sub.2S.sub.2O.sub.4/ OV.sup.2+ -- 200/1/2/0/0.0035/ 10,52- 9
1.499 66 79.74 7/3 NaHCO.sub.3 2.2/0 H.sub.2O/THF 123 CHI.sub.3
Na.sub.2S.sub.2O.sub.4/ OV.sup.2+ -- 200/1/2/0/0.00525/ 9,73- 1
1.474 24 67.21 7/3 NaHCO.sub.3 2.2/0 H.sub.2O/THF 124 CHI.sub.3
Na.sub.2S.sub.2O.sub.4/ OV.sup.2+ -- 200/1/4/0/0.0035/ 9,925- 1.509
24 71.54 7/3 NaHCO.sub.3 2.2/0 H.sub.2O/THF 125 CHI.sub.3
Na.sub.2S.sub.2O.sub.4/ OV.sup.2+ -- 200/1/2/4/0.0035/ 8,903- 1.467
66 71.40 7/3 NaI/ 2.2/0 H.sub.2O/THF NaHCO.sub.3 126 CHI.sub.3
Na.sub.2S.sub.2O.sub.4/ OV.sup.2+ -- 200/1/2/8/0.0035/ 8,915- 1.445
66 69.87 7/3 NaI/ 2.2/0 H.sub.2O/THF NaHCO.sub.3 127 CHI.sub.3
Na.sub.2S.sub.2O.sub.4/ OV.sup.2+ -- 200/1/2/12/0.0035/ 9,81- 9
1.450 66 69.19 7/3 NaI/ 2.2/0 H.sub.2O/THF NaHCO.sub.3 128
CHI.sub.3 Na.sub.2S.sub.2O.sub.4/ OV.sup.2+ -- 200/1/4/8/0.00175/
10,0- 02 1.467 66 75.02 7/3 NaI/ 2.2/0 H.sub.2O/THF NaHCO.sub.3 129
CHI.sub.3 Na.sub.2S.sub.2O.sub.4/ OV.sup.2+ -- 200/1/4/8/0.0035/
11,36- 9 1.495 66 81.95 7/3 NaI/ 2.2/0 H.sub.2O/THF NaHCO.sub.3 130
CHI.sub.3 Na.sub.2S.sub.2O.sub.4/ OV.sup.2+ Brij .RTM. 98
200/1/2/8/0.00175/ 8,961 1.461 66 60.04 7/3 NaI/ 2.2/2180
H.sub.2O/THF NaHCO.sub.3 131 CHI.sub.3 Na.sub.2S.sub.2O.sub.4/
OV.sup.2+ Brij .RTM. 98 200/1/2/4/0.00175/ 7,626 1.512 24 50.24 2/1
NaI/ 2.2/4160 H.sub.2O/THF NaHCO.sub.3 132 CHI.sub.3
Na.sub.2S.sub.2O.sub.4/ OV.sup.2+ -- 200/1/4/8/00035/ 11,482- 1.529
66 85.48 7/3 NaCl/ 2.2/0 H.sub.2O/THF NaHCO.sub.3 133 CHI.sub.3
Na.sub.2S.sub.2O.sub.4/ OV.sup.2+ -- 200/1/2/0/0.0035/ No rxn -- 24
0.0 THF NaHCO.sub.3 2.2/0 134 CHI.sub.3 Na.sub.2S.sub.2O.sub.4/
OV.sup.2+ -- 200/1/2/0/0.0035/ 2,033- 1.623 24 20.11 H.sub.2O
NaHCO.sub.3 2.2/0 135 CHI.sub.3 Na.sub.2S.sub.2O.sub.4/ MV.sup.2+
-- 200/1/2/0/0.0035/ 7,457- 1.489 24 53.58 2/1 NaHCO.sub.3 2.2/0
H.sub.2O/THF 136 CHI.sub.3 Na.sub.2S.sub.2O.sub.4/ MV.sup.2+ --
200/1/2/0/0.0035/ 9,059- 1.455 66 69.01 7/3 NaHCO.sub.3 2.2/0
H.sub.2O/THF 137 CHI.sub.3 Na.sub.2S.sub.2O.sub.4/ MV.sup.2+ --
200/1/2/0/0.0065/ 8,599- 1.455 66 67.82 7/3 NaHCO.sub.3 2.2/0
H.sub.2O/THF 138 CHI.sub.3 Na.sub.2SO.sub.3/ MV.sup.2+ --
200/1/2/0/0.0035/ 2,382 1.746- 66 16.91 7/3 NaHCO.sub.3 2.2/0
H.sub.2O/THF 139 CHI.sub.3 Na.sub.2S.sub.2O.sub.4/ -- Methocel
.RTM. 200/1/2/0/0/ 10,504 1.492 45 78.15 2/1 NaHCO.sub.3 F50
2.2/600.sup.b) H.sub.2O/THF 140 CHI.sub.3 Na.sub.2S.sub.2O.sub.4/
-- Methocel .RTM. 200/1/2/0/0/ 9,644 1.472 45 74.99 2/1 NaHCO.sub.3
F50 2.2/1000.sup.b) H.sub.2O/THF 141 CHI.sub.3
Na.sub.2S.sub.2O.sub.4/ -- NaDDS 200/1/2/0/0/ 3,862 1.795 24- 30.43
2/1 NaHCO.sub.3 2.2/0.1 H.sub.2O/THF 142 CHI.sub.3
Na.sub.2S.sub.2O.sub.4/ -- NaDDS 200/1/2/0/0/ 8,442 1.524 45- 62.93
2/1 NaHCO.sub.3 2.2/3130 H.sub.2O/THF 143 CH.sub.3CH(I)Cl
Na.sub.2S.sub.2O.sub.4/ -- -- 200/1/2/0/0/ 8,945 1.743- 66 60.86
2/1 NaHCO.sub.3 2.2/0 H.sub.2O/THF 144 CH.sub.2I.sub.2
Na.sub.2S.sub.2O.sub.4/ -- -- 200/1/2/0/0/ 8,162 1.861- 66 37.34
2/1 NaHCO.sub.3 2.2/0 H.sub.2O/THF 145 CF.sub.3(CF.sub.2).sub.7
Na.sub.2S.sub.2O.sub.4/ OV.sup.2+ Brij .RTM. 98 200/1/2/0/0.00175/
9,408 2.291 69 3.35 7/3 CH.sub.2CH.sub.2I NaHCO.sub.3 2.2/2180
H.sub.2O/THF 146 CF.sub.3(CF.sub.2).sub.9I Na.sub.2S.sub.2O.sub.4/
OV.sup.2+ -- 200/1/2- /0/0.0035/ 7,554 1.676 24 45.39 7/3
NaHCO.sub.3 2.2/0 H.sub.2O/THF 147 CHBr.sub.3
Na.sub.2S.sub.2O.sub.4/ -- -- 200/1/2/0/0/ 7,943 1.945 45 4- 6.61
2/1 NaHCO.sub.3 2.2/0 H.sub.2O/THF 148 CHBr.sub.3
Na.sub.2S.sub.2O.sub.4/ OV.sup.2+ Brij .RTM. 98 200/1/2/0/0.00175/
6,767 2.033 24 71.52 2/1 NaHCO.sub.3 2.2/4160 H.sub.2O/THF 149
CBr.sub.4 Na.sub.2S.sub.2O.sub.4/ -- -- 200/1/2/0/0/ 6,478 2.150 45
51- .17 2/1 NaHCO.sub.3 2.2/0 H.sub.2O/THF 150 CBr.sub.4
Na.sub.2S.sub.2O.sub.4/ OV.sup.2+ Brij .RTM. 98 200/1/2/0/0.0035/
7,360 2.117 24 50.86 2/1 NaHCO.sub.3 2.2/4160 H.sub.2O/THF 151
CBr.sub.4 Na.sub.2S.sub.2O.sub.8/ -- -- 200/1/2/2/0/ 3,226 2.592 66
16- .59 2/1 HCOONa/ 0/2.2/0 H.sub.2O/THF NaHCO.sub.3 152 CBr.sub.4
Na.sub.2S.sub.2O.sub.8/ -- -- 200/1/2/0/0/ 3,722 2.449 66 21- .61
2/1 NaHCO.sub.3 2.2/0 H.sub.2O/THF 153 CHI.sub.3
Na.sub.2S.sub.2O.sub.3/ -- -- 200/1/2/0/ 0,433 2.551 64 3.12- 2/1
NaHCO.sub.3 2.2/0 H.sub.2O/THF 154 CHI.sub.3
Na.sub.2S.sub.2O.sub.4/ -- NaDDS 200/1/2/0/ 0,400 2.277 12 1- .08
H.sub.2O NaHCO.sub.3 2.2/2085 155 CHI.sub.3 NaNO.sub.2/ -- --
200/1/2/0/ No rxn -- 38 0 2/1 NaHCO.sub.3 2.2/0 H.sub.2O/THF 156
CHI.sub.3 Na.sub.2SO.sub.3/ -- -- 200/1/2/0/ 0,722 2.851 38 14.70
2/1 NaHCO.sub.3 2.2/0 H.sub.2O/THF 157 CHI.sub.3 HCOONa/ -- --
200/1/2/0/0/ No rxn -- 137 0 2/1 NaHCO.sub.3 2.2/0 H.sub.2O/THF 158
CHI.sub.3 NaBH.sub.4/ -- -- 200/1/2/0/0/ 0,624 3.21 137 9.64 2/1
NaHCO.sub.3 2.2/0 H.sub.2O/THF 159 CHI.sub.3 SnCl.sub.22H.sub.2O/
-- -- 200/1/2/0/0/ 0,519 3.818 137 11 2- /1 NaHCO.sub.3 2.2/0
H.sub.2O/THF 160 CHI.sub.3 Na.sub.2S.sub.2O.sub.5/ -- --
200/1/2/0/0/ 0,481 2.458 40 5.- 93 2/1 NaHCO.sub.3 2.2/0
H.sub.2O/THF 161 CHI.sub.3 Na.sub.2S.sub.2O.sub.8/ -- --
200/1/2/2/0/0/ No rxn -- 29 0 2/1 HCOONa/ 2.2/0 H.sub.2O/THF
NaHCO.sub.3 162 CBr.sub.4 Na.sub.2S.sub.2O.sub.8/ -- --
200/1/2/2/0/0/ 4,876 2.331 94 - 36.74 2/1 HCOONa/ 2.2/0
H.sub.2O/THF NaHCO.sub.3 163 CCl.sub.4 Na.sub.2S.sub.2O.sub.8/ --
-- 200/1/2/2/0/0/ 8,757 1.943 92 - 55.38 2/1 HCOONa/ 2.2/0
H.sub.2O/THF NaHCO.sub.3 164 CHI.sub.3 HOCH.sub.2SO.sub.2 -- --
200/1/2/0/0/ 0,732 2.568 58 7.11 2/- 1 Na2H.sub.2O/ 2.2/0
H.sub.2O/THF NaHCO.sub.3 165 CHI.sub.3 HOCH.sub.2SO.sub.3 -- --
200/1/2/0/0/ 0,488 2.609 58 7.34 2/- 1 Na/ 2.2/0 H.sub.2O/THF
NaHCO.sub.3 166 CHI.sub.3 H.sub.2NC(.dbd.NH) -- -- 200/1/2/0/0/
7,407 1.509 58 55.84 2- /1 SO.sub.2H/ 2.2/0 H.sub.2O/THF
NaHCO.sub.3 .sup.a)Ratio [VC]/[initiator]/[catalyst]/[electron
shuttle]/[buffer]/[surfactant] mol/mol/mol/mol/mol/ppm w/w to
monomer
Table 1 presents selected examples of Fe(O) catalyzed VC
polymerization. Examples 1 to 9 describe the initiation performed
from .alpha.-haloesters. Example 9 describes the synthesis of a
block copolymer by initiating from the Cl chain end of PMMA
synthesized via living radical polymerization. Examples 10 to 16
describe the VC polymerization initiated from benzyl halides and
pseudohalides, while examples 17 and 18 exemplify
.alpha.-cyanoesters and example 19 describes the use of sulfonyl
halides as initiators. The polymerization may be performed in
o-DCB, THF or DMF. In o-DCB, at constant [VC]:[I]:[C]:[L] ratios,
lower temperatures lead to higher molecular weights and narrower
Mw/Mn but lower conversions (#4 6).
Table 2 presents the TiCp.sub.2Cl.sub.2 catalyzed polymerization of
VC initiated from various halides. By itself, in the absence of
added initiator, TiCp.sub.2Cl.sub.2 catalyzes VC polymerization
only to very low conversion. Polymers can be obtained in the
presence of .alpha.-haloesters (examples 21 to 25), benzy halides
and pseudohalides (examples 26 to 31), .alpha.-cyanoesters (example
32) as well as imidyl halides (examples 33 and 34). The addition of
Al.sup.iBu.sub.3 (examples 23 and 25) significantly increase the
conversion. Star polymers can be synthesized in the presence of
trifunctional initiators (example 27). Lower temperature affords
higher Mn but lower conversion (examples 21 and 22). For Ti based
catalysts, bhlorine and bromine containing initiators generate
higher conversions than iodine initiators and are therefore
preferred.
Table 3 presents the Cu(I) catalyzed polymerization of VC initiated
from various halides. In the presence of more activating ligands
than bpy, such as Me.sub.6-TREN, CuBr can catalyzed VC
polymerization initiated from .alpha.-haloesters (examples 37 and
38). More reactive Cu(l) species such as CuC.dbd.C-Ph, CuSPh or
Cu.sub.2Te (examples 39, 40 and 46) can catalyze VC polymerization
even in the presence of bpy as ligand. For the less reactive copper
halides, the presence of more activating polyamine ligands is
therefore necessary.
Table 4 presents the Cu(O) catalyzed polymerization of VC initiated
from various halides. Initiation from allyl chloride defects is
demonstrated using various haloallyl model compounds (examples 48
50) while the initiation from the repeat unit of PVC is
demonstrated with the corresponding 1,1-dichloro (example 53),
1,1-chlorobromo (example 67) and 1,1-chloroiodo derivatives
(examples 92 to 117). Cu(O) is also able to catalyze VC
polymerization in the presence of a large variety of chloro, bromo
and iodo initiators such as .alpha.-cyanohalides (examples 51 and
52), .alpha.-haloesters (examples 57 59, 61 66 and 72 74) and
various benzyl halides such as .alpha.,.alpha.'-dichloro-p-xylene
(examples 54 56), .alpha.,.alpha.'-dibromo-p-xylene (example 70)
1-bromo-1-phenylethane (examples 68 and 69) and
1,2,4,5-tetrakisbromomethyl benzene (example 60, star polymer),
.alpha.,.alpha.'-diiodo-p-xylene (examples 118 to 137). Other
successful initiators include perfloroalkyliodides (example 75),
allyl iodide (examples 76 to 79), iodoform (examples 80 to 89) and
carbon tetraiodide (examples 90 and 91).
The experiments described in examples 125 132 are plotted in FIG. 1
and show that the molecular weight increases linearly with
conversion while the polydispersity decreases with conversion at
130.degree. C. using o-DCB as solvent. A linear (FIG. 2) dependence
between molecular weight and conversion is observed (examples 114
117) even at 90.degree. C. if VC polymerization is carried out in
water in the presence of a surfactant (sodium dodecylsulfate).
The results from examples 97 to 108 describe the combined effect of
VC concentration (from bulk 14.4 M to solution 4.8 M) and
temperature (from 60.degree. C. to 130.degree. C.) on the molecular
weight molecular weight distribution and conversion of the
resulting PVC for a reaction time of 20 h and are presented in FIG.
3. An optimum conversion is observed for [VC]=7.2 M while bulk
polymerization generates both lower conversion as well as lower
molecular weight and broader molecular weight distribution.
Table 5 presents miscellaneous examples of metal catalyzed VC
polymerization. It was observed that .alpha.-haloesters catalyze VC
polymerization (examples 140 144) in the presence of Al(O)/bpy and
Al.sup.iBu.sub.3 as well as Cd(O)/bpy, Sm(O)/bpy and Zn(O)/bpy.
.alpha.-Cyanohalides (example 145) can catalyze VC polymerization
in the presence of Cr(CO).sub.6.
Table 6 presents selected examples of the room temperature metal
catalyzed VC polymerization in water, organic solvents or mixtures
thereof. In the presence of activating ligands such as TREN, Cu(O)
and its derivatives are successful in polymerizing VC at room
temperature. Particularly suitable initiators include iodine
derivatives such as CH.sub.3--CH(Cl)--I (example 147 to example
178), CHI.sub.3 (example 179 to example 227),
CF.sub.3--(CF.sub.2).sub.9--I (example 228),
CH.sub.2.dbd.CH--CH.sub.2--I (example 229) and
I--CH.sub.2-Ph-CH.sub.2--I (example 233). A demonstration of the
Cu(O)/TREN catalyzed living radical polymerization of VC at room
temperature initiated from CH.sub.3--CH(Cl)--I in water is
presented in FIG. 4. A linear dependence between molecular weight
and conversion is observed up to complete conversion of VC.
Initiators that generate high Mn PVC at room temperature are also
bromine and chlorine containing initiators such as
BrC(CH.sub.3).sub.2--COO-Ph-Ph-OCO--C(CH.sub.3).sub.2Br (example
230) or CH.sub.3C[Ph-OCO--C(CH.sub.3).sub.2Br].sub.3 (example 231
in which case a star PVC polymer was obtained) or
Cl--CH.sub.2-Ph-CH.sub.2--Cl (example 232). Low Mn PVC synthesized
by living radical polymerization (example 235) can be
chain-extended with VC in water while commercial PVC (example 236)
can be grafted in water with VC under the same conditions. Very
suitable catalytic systems include Cu(O)/TREN, Cu.sub.2Te/TREN and
combinations thereof. By contrast with the solution experiments
performed with CuX (X=Cl, Br, I) at higher temperatures, the
CuX/TREN catalytic systems are active in water even at room
temperature (examples 173 177, 232). A conventional initiator such
as benzoyl peroxide can be employed as well (example 234). The
polymerization can also be carried out at room temperature in
various organic solvents such as o-DCB, THF, Acetone, Ethyl
Acetate, MeOH etc or mixtures water/organic solvent in which case
the presence of the surfactant may be not be necessary.
Table 7 presents selected examples of
Na.sub.2S.sub.2O.sub.4-catalyzed LRP of VC initiated with iodoform
in H.sub.2O/THF. Examples 1 22 with the same water-THF ratio 2/1
are plotted in FIG. 1. The two rate constants are observed.
k.sub.p1 represents a liquid-liquid emulsion polymerization when
k.sub.p2 represents a solid-liquid suspension one. Such a transfer
takes place after about 24 h at about 60% of VC conversion.
k.sub.p1>k.sub.p2 more than 2 times (0.0039 h.sup.-1 and 0.0015
h.sup.-1 respectively). M.sub.n is consistent with M.sub.th as for
a living process. Polydispersity drastically decreases in the
beginning of the polymerization with increasing of M.sub.th and
keeps lower than 1.5 until the end of the process after 66 h
(example 19). VC conversion at this point is a little more than
80%. Example 22 without buffer shows low conversion. Change of the
H.sub.2O/THF ratio to 7/3 (example 23) does not have a significant
influence on this reaction.
Table 8 presents room temperature Na.sub.2S.sub.2O.sub.4-catalyzed
LRP of VC initiated with iodoform in H.sub.2O/THF in the presence
of surfactant Brij.RTM. 98. These experiments were carried out with
different H.sub.2O/THF ratios both 2/1 and 7/3. Comparison of the
experiments, for example, 47 and 48, which are equal except for
H.sub.2O/THF ratios (7/3 and 2/1 resp.) shows a little higher yield
(80 vs. 78%) and lower polydispersity (1.54 vs. 1.55) for the
former one after 66 h. Amount of the surfactant varies from 2080 to
16640 ppm w/w relative to VC. Comparing the results of the
experiments 26, 54, 55, 56 and 58 for 45 h one can see the
increasing of polydispersity with increasing of surfactant amount
from 1.48 to 1.66, when the VC conversions do not differ
essentially each from others. The experiments with H.sub.2O/THF
ratio 7/3 and amount of Brij.RTM. 98 2080 ppm w/w relative to VC
are plotted in FIG. 2. One can also observe two different
polymerization rates, namely for emulsion and suspension. In this
case k.sub.p1 for the liquid-liquid emulsion polymerization is
higher then that rate constant for the non-surfactant process in
FIG. 1 (0.050 vs. 0.039 h.sup.-1), whereas the two constants
k.sub.p2 are similar (0.013 and 0.015 h.sup.-1 respectively). The
emulsion-suspension transfer also occurs after about 24 h but
already at about 70% of VC conversion. The emulsion is kept longer
in this case. M.sub.n is in good agreement with M.sub.th.
Polydispersity drops fast from 2.4 to less than 1.5 and is held
practically constant up to the end of polymerization.
Table 9 presents results of the room temperature
Na.sub.2S.sub.2O.sub.4-catalyzed LRP of VC initiated with iodoform
in H.sub.2O/THF in the presence of electron shuttle OV.sup.2+ and
surfactant Brij.RTM. 98. All other factors being equal, decreasing
of OV.sup.2+ decreases polydispersity from 1.49 to 1.48
(experiments 72 and 67) while the monomer conversions are equal
(72%). Increasing of surfactant amount increases monomer conversion
but also polydispersity (experiments 71 and 74). Experiments 59 70
are plotted in FIG. 3. One can see that the rate constant of
emulsion polymerizationand k.sub.p1 is the highest 0.066 h.sup.-1
and the emulsion-suspension transfer occurs at above 70% of monomer
conversion after less than 20 h, while the constant of solid-liquid
polymerization k.sub.p2 is lower. As in the previous cases M.sub.n
is consistent with M.sub.th and polydispersity decreases up to 1.5
with increasing of M.sub.th up to about 6000 and then is kept close
to this value. Monomer conversion is 82% after 66 h.
Table 10 presents results of the room temperature
Na.sub.2S.sub.2O.sub.4-catalyzed LRP of VC initiated with iodoform
in H.sub.2O/THF in the presence of electron shuttle MV.sup.2+ and
surfactant Brij.RTM. 98. Experiments 99, 98 demonstrate a very
small increasing of polydispersity from 1.55 to 1.56 with
increasing of surfactant amount, while monomer conversions are
practically equal (70 and 71% resp.). A marked increase of
MV.sup.2+ (experiment 101) lows the conversion (36%) and shows an
increase in polydispersity (1.73) in comparison with lower amounts
of methyl viologen (experiments 89, 96, 97, 100). Experiments 81 95
are plotted in FIG. 4. As one can see MV.sup.2+ accelerates
liquid-liquid emulsion polymerization k.sub.p1=0.054 h.sup.-1,
while k.sub.p2 is smaller than for the non-electron shuttle
involving reactions but bigger than for one of octyl viologen.
Dependence M.sub.n on M.sub.th is similar as for the previous cases
as well as polydispersity is.
Tables 11 and 12 along with FIGS. 5 and 6 present
Na.sub.2S.sub.2O.sub.8--HCOONa-catalyzed radical polymerization of
VC initiated with, respectively, bromoform and chloroform in
H.sub.2O/THF. These polymerizations occur only in the presence of
no-iodine containing initiators and show a typical free radical
dependence M.sub.n on M.sub.th as it can be seen from FIGS. 9 and
10.
Table 13 presents room temperature
H.sub.2NC(.dbd.NH)SO.sub.2H-catalyzed LRP of VC initiated with
iodoform in H.sub.2O/THF in the presence of electron shuttle
OV.sup.2+. As H.sub.2NC(.dbd.NH)SO.sub.2H is an acidic compound
twice amount of buffer is used. The results of the experiments are
plotted in FIG. 7. Both k.sub.p1 and k.sub.p2 are lower than for a
dithionite-mediated polymerization. Maximal conversion is below
60%. M.sub.n shows an ideal dependence on M.sub.th. Polydispersity
decreases from 1.9 to 1.5.
Table 14 presents selected examples of the room temperature
non-metallic SET reagents-mediated LRP of VC in H.sub.2O, THF and
mixtures thereof. The role of the solvent is illustrated by
experiments 133, 134 and 154. While in water either in the presence
of OV.sup.2+ or NaDDS reaction occurs there is no
dithionite-catalyzed reaction in dry THF. Different halogen
containing compounds, other than iodoform, in conjunction with
Na.sub.2S.sub.2O.sub.4 can initiate VC polymerization (experiments
143, 144, 145, 146, 149) both in the presence of electron shuttle
and surfactant and without them. The CO.sub.2.sup.- radical anion
precursor Na.sub.2S.sub.2O.sub.8--HCOONa is active in conjunction
with bromo- or chloro-containing initiators (experiments 151, 152,
162, 163). Different SO.sub.2 containing compounds other than
Na.sub.2S.sub.2O.sub.4 show activity with iodoform as initiator
(experiments 152, 156, 160, 164, 165, 166). Some surfactants show
activity in experiments 139, 140, 141, 142, 154. Additives such as
sodium halides are active (experiments 125 132), with the narrowest
polydispersity (1.445) and high yeld obtained in experiment
126.
Examples of Preparation of the Chlorine Containing Polymer
Utilizing a Metallic Catalyst
The polymerizations reported were performed as follows unless
otherwise noted: A 50 mL Ace Glass 8648 #15 Ace-Thred pressure tube
equipped with bushing and plunger valve containing solvent
(ortho-dichlorobenzene, 10 mL), initiator catalyst, ligand,
optional additive and vinyl chloride (5 mL, 0.072 mol), was
degassed by three freeze-vacuum pump-thaw cycles was filled with
argon. The reaction mixture was slowly heated to the specific
reaction temperature in an oil bath. After the specific reaction
time, the tube was slowly cooled and excess vinyl chloride was
allowed to boil off. Methylene chloride (10 mL) was added and the
solution was precipitated into methanol, filtered and dried. The
conversion was determined gravimetrically and the number average
molecular weight (Mn) and molecular weight distribution (Mw/Mn)
were determined by gel permeation chromatography using a
calibration based on polystyrene standards. GPC analysis of the
polymers was performed on a Perkin-Elmer Series 10 high pressure
liquid chromatograph equipped with an LC-100 column oven
(22.degree. C.), a Nelson Analytical 900 Series integrator data
station, a Perkin-Elmer 785A UV/Visible Detector (254 nm), a Varian
Star 4090 RI detector and 2 AM gel (10 .mu.m, 500 .ANG. and 10
.mu.m, 10.sup.4 .ANG.) columns. THF (Fisher, HPLC-grade) was used
as eluent at a flow rate of 1 mL/min.
A number of polymerization reactions were produced in accordance
with the above description. Selected examples from the Tables 1 6
are presented below:
Table 1, Example 1
A 50 mL Ace Glass 8648 #15 Ace-Thred pressure tube equipped with
bushing and plunger valve containing vinyl chloride (5 mL, 0.072
mol), solvent (ortho-dichlorobenzene (o-DCB), 10 mL), initiator
(ethyl 2-bromoisobutyrate, 223 mg, 1.12 mmol), catalyst (Fe(O), 40
mg, 0.7 mmol) and ligand (phen 200 mg, 1.1 mmol) was degassed by
three freeze-vacuum pump-thaw cycles and filled with argon. The
reaction mixture was slowly heated to 90.degree. C. in an oil bath.
After 19 hours, the tube was slowly cooled and excess vinyl
chloride was allowed to boil off. Methylene chloride (10 mL) was
added and the solution was precipitated into methanol, filtered and
dried to yield 1.17 g (26%) of PVC, Mn=10,000, Mw/Mn=1.66.
Table 1, Example 9
A 50 mL Ace Glass 8648 #15 Ace-Thred pressure tube equipped with
bushing and plunger valve containing vinyl chloride (5 mL, 0.072
mol), solvent (o-DCB, 10 mL), initiator (chlorine terminated
poly(methylmethacrylate) PMMA-CH.sub.2--C(COOMe)(CH.sub.3)--Cl,
Mn=6,300, Mw/Mn=1.25, 1 g, 0.16 mmol), catalyst (Fe(O), 40 mg, 0.7
mmol) and ligand (phen 100 mg, 0.55 mmol) was degassed by three
freeze-vacuum pump-thaw cycles and filled with argon. The reaction
mixture was slowly heated to 90.degree. C. in an oil bath. After 20
hours, the tube was slowly cooled and excess vinyl chloride was
allowed to boil off. Methylene chloride (20 mL) was added and the
solution was precipitated into methanol, filtered and dried to
yield 3.5 g (35%) of PVC, Mn=8,300, Mw/Mn=1.73.
Table 1, Example 18
A 50 mL Ace Glass 8648 #15 Ace-Thred pressure tube equipped with
bushing and plunger valve containing vinyl chloride (5 mL, 0.072
mol), solvent (o-DCB, 10 mL), initiator (1-chloro-1-cyanoethane, 79
mg, 0.56 mmol), catalyst (Fe(CO).sub.5, 133 mg, 0.68 mmol) was
degassed by three freeze-vacuum pump-thaw cycles and filled with
argon. The reaction mixture was slowly heated to 90.degree. C. in
an oil bath. After 18 hours, the tube was slowly cooled and excess
vinyl chloride was allowed to boil off. Methylene chloride (10 mL)
was added and the solution was precipitated into methanol, filtered
and dried to yield 0.23 g (4%) of PVC, Mn=14,300, Mw/Mn=1.65.
Table 1, Example 19
A 50 mL Ace Glass 8648 #15 Ace-Thred pressure tube equipped with
bushing and plunger valve containing vinyl chloride (5 mL, 0.072
mol), solvent (o-DCB, 10 mL), initiator (4-florobenzenesulfonyl
chloride 132 mg, 0.56 mmol), catalyst (Fe(O), 40 mg, 0.7 mmol) )
and ligand (phen 200 mg, 1.12 mmol) was degassed by three
freeze-vacuum pump-thaw cycles and filled with argon. The reaction
mixture was slowly heated to 90.degree. C. in an oil bath. After 18
hours, the tube was slowly cooled and excess vinyl chloride was
allowed to boil off. Methylene chloride (10 mL) was added and the
solution was precipitated into methanol, filtered and dried to
yield 1 g (22%) of PVC, Mn=14,300, Mw/Mn=1.82.
Table 2, Example 21
A 50 mL Ace Glass 8648 #15 Ace-Thred pressure tube equipped with
bushing and plunger valve containing vinyl chloride (5 mL, 0.072
mol), solvent (o-DCB, 10 mL), initiator (ethyl 2-bromoisobutyrate,
111 mg, 0.56 mmol) and catalyst (TiCp.sub.2Cl.sub.2, 167 mg, 0.67
mmol) was degassed by three freeze-vacuum pump-thaw cycles and
filled with argon. The reaction mixture was slowly heated to
90.degree. C. in an oil bath. After 22 hours, the tube was slowly
cooled and excess vinyl chloride was allowed to boil off. Methylene
chloride (10 mL) was added and the solution was precipitated into
methanol, filtered and dried to yield 0.47 g (10%) of PVC,
Mn=14,300, Mw/Mn=1.82.
Table 2, Example 23
A 50 mL Ace Glass 8648 #15 Ace-Thred pressure tube equipped with
bushing and plunger valve containing vinyl chloride (5 mL, 0.072
mol), solvent (o-DCB, 10 mL), initiator (ethyl 2-bromoisobutyrate,
111 mg, 0.56 mmol), catalyst (TiCp.sub.2Cl.sub.2, 167 mg, 0.6 mmol)
and additive (Al.sup.iBu.sub.3, 2 mmol, 2 mL 1M in toluene) was
degassed by three freeze-vacuum pump-thaw cycles and filled with
argon. The reaction mixture was slowly heated to 90.degree. C. in
an oil bath. After 17 hours, the tube was slowly cooled and excess
vinyl chloride was allowed to boil off. Methylene chloride (10 mL)
was added and the solution was precipitated into methanol, filtered
and dried to yield 2.8 g (60%) of PVC, Mn=3,800, Mw/Mn=2.10.
Table 2, Example 24
A 50 mL Ace Glass 8648 #15 Ace-Thred pressure tube equipped with
bushing and plunger valve containing vinyl chloride (5 mL, 0.072
mol), solvent (o-DCB, 10 mL), initiator (ethyl 2-bromoisobutyrate,
111 mg, 0.56 mmol), catalyst (TiCp.sub.2Cl.sub.2, 167 mg, 0.6
mmol), additive (Zn(O), 65 mg, 1 mmol) and ligand (bpy 100 mg, 0.4
mmol) was degassed by three freeze-vacuum pump-thaw cycles and
filled with argon. The reaction mixture was slowly heated to
90.degree. C. in an oil bath. After 17 hours, the tube was slowly
cooled and excess vinyl chloride was allowed to boil off. Methylene
chloride (10 mL) was added and the solution was precipitated into
methanol, filtered and dried to yield 1 g (22%) of PVC, Mn=14,800,
Mw/Mn=1.95.
Table 2, Example 25
A 50 mL Ace Glass 8648 #15 Ace-Thred pressure tube equipped with
bushing and plunger valve containing vinyl chloride (5 mL, 0.072
mol), solvent (o-DCB, 10 mL), initiator (ethyl 2-bromoisobutyrate,
111 mg, 0.56 mmol), catalyst (Ti(OBu).sub.4, 231 mg, 0.7 mmol),
additive (Al.sup.iBu.sub.3, 2 mmol, 2 mL 1M in toluene) was
degassed by three freeze-vacuum pump-thaw cycles and filled with
argon. The reaction mixture was slowly heated to 90.degree. C. in
an oil bath. After 17 hours, the tube was slowly cooled and excess
vinyl chloride was allowed to boil off. Methylene chloride (10 mL)
was added and the solution was precipitated into methanol, filtered
and dried to yield 4 g (88%) of PVC, Mn=14,800 Mw/Mn=1.95.
Table 2, Example 29
A 50 mL Ace Glass 8648 #15 Ace-Thred pressure tube equipped with
bushing and plunger valve containing vinyl chloride (5 mL, 0.072
mol), solvent (o-DCB, 10 mL), initiator
(.alpha.,.alpha.'-dichloro-p-xylene, 25 mg 0.14 mmol) and catalyst
(TiCp.sub.2Cl.sub.2, 70 mg, 0.28 mmol), was degassed by three
freeze-vacuum pump-thaw cycles and filled with argon. The reaction
mixture was slowly heated to 130.degree. C. in an oil bath. After
20 hours, the tube was slowly cooled and excess vinyl chloride was
allowed to boil off. Methylene chloride (10 mL) was added and the
solution was precipitated into methanol, filtered and dried to
yield 1.25 g (28%) of PVC, Mn=4,900, Mw/Mn=1.81.
Table 2, Example 33
A 50 mL Ace Glass 8648 #15 Ace-Thred pressure tube equipped with
bushing and plunger valve containing vinyl chloride (5 mL, 0.072
mol), solvent (o-DCB, 10 mL), initiator (N-bromosuccinimide, 100 mg
0.56 mmol) and catalyst (TiCp.sub.2Cl.sub.2, 170 mg, 0.68 mmol),
was degassed by three freeze-vacuum pump-thaw cycles and filled
with argon. The reaction mixture was slowly heated to 90.degree. C.
in an oil bath. After 19 hours, the tube was slowly cooled and
excess vinyl chloride was allowed to boil off. Methylene chloride
(10 mL) was added and the solution was precipitated into methanol,
filtered and dried to yield 0.2 g (4%) of PVC, Mn=19,000
Mw/Mn=1.78.
Table 2, Example 34
A 50 mL Ace Glass 8648 #15 Ace-Thred pressure tube equipped with
bushing and plunger valve containing vinyl chloride (5 mL, 0.072
mol), solvent (o-DCB, 10 mL), initiator (trichloroisocyanuric acid,
100 mg, 0.56 mmol) and catalyst (TiCp.sub.2Cl.sub.2, 170 mg, 0.68
mmol), was degassed by three freeze-vacuum pump-thaw cycles and
filled with argon. The reaction mixture was slowly heated to
90.degree. C. in an oil bath. After 19 hours, the tube was slowly
cooled and excess vinyl chloride was allowed to boil off. Methylene
chloride (10 mL) was added and the solution was precipitated into
methanol, filtered and dried to yield 0.2 g (4%) of PVC, Mn=19,000,
Mw/Mn=1.80.
Table 2, Example 35
A 50 mL Ace Glass 8648 #15 Ace-Thred pressure tube equipped with
bushing and plunger valve containing vinyl chloride (5 mL, 0.072
mol), solvent (o-DCB, 10 mL), initiator
(1,1,1-tris(4-chlorosulfonylphenyl)ethane,100 mg, 0.18 mmol) and
catalyst (TiCp.sub.2Cl.sub.2, 400 mg, 1.6 mmol), was degassed by
three freeze-vacuum pump-thaw cycles and filled with argon. The
reaction mixture was slowly heated to 110.degree. C. in an oil
bath. After 22 hours, the tube was slowly cooled and excess vinyl
chloride was allowed to boil off. Methylene chloride (10 mL) was
added and the solution was precipitated into methanol, filtered and
dried to yield 0.35 g (7%) of PVC, Mn=4,000 Mw/Mn=2.05.
Table 3, Example 39
A 50 mL Ace Glass 8648 #15 Ace-Thred pressure tube equipped with
bushing and plunger valve containing vinyl chloride (5 mL, 0.072
mol), solvent (DMF, 5 mL), initiator (1-chloro-1-cyanoethane, 64
mg, 0.72 mmol) catalyst (copper phenylacetylide, 178 mg, 1.1 mmol)
and ligand (bpy, 337 mg, 2.16 mmol) was degassed by three
freeze-vacuum pump-thaw cycles and filled with argon. The reaction
mixture was slowly heated to 90.degree. C. in an oil bath. After 19
hours, the tube was slowly cooled and excess vinyl chloride was
allowed to boil off. Methylene chloride (10 mL) was added and the
solution was precipitated into methanol, filtered and dried to
yield 0.67 g (15%) of PVC, Mn=1,300, Mw/Mn=3.60.
Table 3, Example 40
A 50 mL Ace Glass 8648 #15 Ace-Thred pressure tube equipped with
bushing and plunger valve containing vinyl chloride (5 mL, 0.072
mol), solvent (DMF, 5 mL), initiator (1-chloro-1-cyanoethane, 51
mg, 0.56 mmol) catalyst (copper thiophenoxide, 69 mg, 0.4 mmol) and
ligand (bpy, 337 mg, 2.16 mmol) was degassed by three freeze-vacuum
pump-thaw cycles and filled with argon. The reaction mixture was
slowly heated to 60.degree. C. in an oil bath. After 19 hours, the
tube was slowly cooled and excess vinyl chloride was allowed to
boil off. Methylene chloride (10 mL) was added and the solution was
precipitated into methanol, filtered and dried to yield 0.6 g (13%)
of PVC, Mn=2,800, Mw/Mn=3.60.
Table 3, Example 41
A 50 mL Ace Glass 8648 #15 Ace-Thred pressure tube equipped with
bushing and plunger valve containing vinyl chloride (5 mL, 0.072
mol), solvent (o-DCB, 5 mL), initiator (1-chloro-1-iodoethane, 53
mg, 0.28 mmol) catalyst (copper (I) bromide, 61 mg, 0.42 mmol) and
ligand (tris[2-(dimethylamino)ethyl]amine (Me.sub.6-TREN), 193 mg,
0.84 mmol) was degassed by three freeze-vacuum pump-thaw cycles and
filled with argon. The reaction mixture was slowly heated to
90.degree. C. in an oil bath. After 44 hours, the tube was slowly
cooled and excess vinyl chloride was allowed to boil off. Methylene
chloride (10 mL) was added and the solution was precipitated into
methanol, filtered and dried to yield 0.22 g (5%) of PVC, Mn=3,200,
Mw/Mn=1.30.
Table 3, Example 46
A 50 mL Ace Glass 8648 #15 Ace-Thred pressure tube equipped with
bushing and plunger valve containing vinyl chloride (5 mL, 0.072
mol), solvent (o-DCB, 5 mL), initiator
(.alpha.,.alpha.'-dithiocyanato-p-xylene, 61 mg, 0.28 mmol)
catalyst (copper (I) telluride, 285 mg, 1.12 mmol) and ligand (bpy,
350 mg, 1.36 mmol) was degassed by three freeze-vacuum pump-thaw
cycles and filled with argon. The reaction mixture was slowly
heated to 130.degree. C. in an oil bath. After 22 hours, the tube
was slowly cooled and excess vinyl chloride was allowed to boil
off. Methylene chloride (10 mL) was added and the solution was
precipitated into methanol, filtered and dried to yield 0.36 g (8%)
of PVC, Mn=5,100, Mw/Mn=2.23.
Table 4, Example 48
A 50 mL Ace Glass 8648 #15 Ace-Thred pressure tube equipped with
bushing and plunger valve containing vinyl chloride (5 mL, 0.072
mol), solvent (o-DCB, 10 mL), initiator
(3-chloro-2-chloromethylpropene, 90 mg, 0.72 mmol) catalyst
(copper, 184 mg, 2.8 mmol) and ligand (bpy, 898 mg, 5.76 mmol) was
degassed by three freeze-vacuum pump-thaw cycles and filled with
argon. The reaction mixture was slowly heated to 130.degree. C. in
an oil bath. After 20 hours, the tube was slowly cooled and excess
vinyl chloride was allowed to boil off. Methylene chloride (10 mL)
was added and the solution was precipitated into methanol, filtered
and dried to yield 1.4 g (31%) of PVC, Mn=7,700, Mw/Mn=1.85.
Table 4, Example 49
A 50 mL Ace Glass 8648 #15 Ace-Thred pressure tube equipped with
bushing and plunger valve containing vinyl chloride (5 mL, 0.072
mol), solvent (o-DCB, 10 mL), initiator (1-chloro-methyl-2-butene,
75 mg, 0.72 mmol) catalyst (copper, 92 mg, 1.4 mmol) and ligand
(bpy, 450 mg, 2.88 mmol) was degassed by three freeze-vacuum
pump-thaw cycles and filled with argon. The reaction mixture was
slowly heated to 130.degree. C. in an oil bath. After 20 hours, the
tube was slowly cooled and excess vinyl chloride was allowed to
boil off. Methylene chloride (10 mL) was added and the solution was
precipitated into methanol, filtered and dried to yield 0.9 g (20%)
of PVC, Mn=8,300, Mw/Mn=1.62.
Table 4, Example 49
A 50 mL Ace Glass 8648 #15 Ace-Thred pressure tube equipped with
bushing and plunger valve containing vinyl chloride (5 mL, 0.072
mol), solvent (o-DCB, 10 mL), initiator (1-chloro-methyl-2-butene,
75 mg, 0.72 mmol), catalyst (copper, 92 mg, 1.4 mmol) and ligand
(bpy, 450 mg, 2.88 mmol) was degassed by three freeze-vacuum
pump-thaw cycles and filled with argon. The reaction mixture was
slowly heated to 130.degree. C. in an oil bath. After 20 hours, the
tube was slowly cooled and excess vinyl chloride was allowed to
boil off. Methylene chloride (10 mL) was added and the solution was
precipitated into methanol, filtered and dried to yield 0.9 g (20%)
of PVC, Mn=8,300, Mw/Mn=1.62.
Table 4, Example 50
A 50 mL Ace Glass 8648 #15 Ace-Thred pressure tube equipped with
bushing and plunger valve containing vinyl chloride (5 mL, 0.072
mol), solvent (o-DCB, 10 mL), initiator (allyl chloride, 55 mg,
0.72 mmol), catalyst (copper, 92 mg, 1.4 mmol) and ligand (bpy, 450
mg, 2.88 mmol) was degassed by three freeze-vacuum pump-thaw cycles
and filled with argon. The reaction mixture was slowly heated to
130.degree. C. in an oil bath. After 20 hours, the tube was slowly
cooled and excess vinyl chloride was allowed to boil off. Methylene
chloride (10 mL) was added and the solution was precipitated into
methanol, filtered and dried to yield 1.2 g (27%) of PVC, Mn=6,100,
Mw/Mn=1.83.
Table 4, Example 53
A 50 mL Ace Glass 8648 #15 Ace-Thred pressure tube equipped with
bushing and plunger valve containing vinyl chloride (5 mL, 0.072
mol), solvent (o-DCB, 10 mL), initiator (methylene chloride, 61 mg,
0.72 mmol), catalyst (copper, 92 mg, 1.4 mmol) and ligand (bpy, 450
mg, 2.88 mmol) was degassed by three freeze-vacuum pump-thaw cycles
and filled with argon. The reaction mixture was slowly heated to
130.degree. C. in an oil bath. After 20 hours, the tube was slowly
cooled and excess vinyl chloride was allowed to boil off. Methylene
chloride (10 mL) was added and the solution was precipitated into
methanol, filtered and dried to yield 0.25 g (5%) of PVC,
Mn=50,000, Mw/Mn=2.75.
Table 4, Example 55
A 50 mL Ace Glass 8648 #15 Ace-Thred pressure tube equipped with
bushing and plunger valve containing vinyl chloride (5 mL, 0.072
mol), solvent (o-DCB, 10 mL), initiator
(.alpha.,.alpha.'-dichloro-p-xylene, 12 mg, 0.07 mmol), catalyst
(copper, 36 mg, 0.56 mmol) and ligand (bpy, 175 mg, 1.12 mmol) was
degassed by three freeze-vacuum pump-thaw cycles and filled with
argon. The reaction mixture was slowly heated to 130.degree. C. in
an oil bath. After 21 hours, the tube was slowly cooled and excess
vinyl chloride was allowed to boil off. Methylene chloride (10 mL)
was added and the solution was precipitated into methanol, filtered
and dried to yield 0.8 g (18%) of PVC, Mn=22,400, Mw/Mn=1.53.
Table 4, Example 56
A 50 mL Ace Glass 8648 #15 Ace-Thred pressure tube equipped with
bushing and plunger valve containing vinyl chloride (2.5 mL, 0.036
mol), solvent (o-DCB, 5 mL), initiator
(.alpha.,.alpha.'-dichloro-p-xylene, 105 mg, 0.6 mmol), catalyst
(copper, 307 mg, 0.48 mmol) and ligand (bpy, 750 mg, 0.48 mmol) was
degassed by three freeze-vacuum pump-thaw cycles and filled with
argon. The reaction mixture was slowly heated to 130.degree. C. in
an oil bath. After 20 hours, the tube was slowly cooled and excess
vinyl chloride was allowed to boil off. Methylene chloride (10 mL)
was added and the mixture was precipitated into methanol, filtered
and dried to yield 2.3 g (95%) of PVC.
Table 4, Example 57
A 50 mL Ace Glass 8648 #15 Ace-Thred pressure tube equipped with
bushing and plunger valve containing vinyl chloride (5 mL, 0.072
mol), solvent (o-DCB, 10 mL), initiator (2-bromo-2-methylpropionyl
bromide, 64 mg, 0.28 mmol), catalyst (copper, 72 mg, 1.12 mmol) and
ligand (bpy, 350 mg, 2.24 mmol) was degassed by three freeze-vacuum
pump-thaw cycles and filled with argon. The reaction mixture was
slowly heated to 90.degree. C. in an oil bath. After 22 hours, the
tube was slowly cooled and excess vinyl chloride was allowed to
boil off. Methylene chloride (10 mL) was added and the solution was
precipitated into methanol, filtered and dried to yield 0.5 g (12%)
of PVC, Mn=17,000, Mw/Mn=1.90.
Table 4, Example 59
A 50 mL Ace Glass 8648 #15 Ace-Thred pressure tube equipped with
bushing and plunger valve containing vinyl chloride (5 mL, 0.072
mol), solvent (o-DCB, 10 mL), initiator (ethyl 2-bromoisobutyrate,
111 mg, 0.6 mmol), catalyst (copper, 40 mg, 0.6 mmol) ligand (bpy,
150 mg, 0.96 mmol) and additive (Al.sup.iBu.sub.3, 0.6 mmol, 0.6 mL
1M in toluene) was degassed by three freeze-vacuum pump-thaw cycles
and filled with argon. The reaction mixture was slowly heated to
90.degree. C. in an oil bath. After 22 hours, the tube was slowly
cooled and excess vinyl chloride was allowed to boil off. Methylene
chloride (10 mL) was added and the solution was precipitated into
methanol, filtered and dried to yield 3.5 g (77%) of PVC, Mn=6,400,
Mw/Mn=1.85.
Table 4, Example 60
A 50 mL Ace Glass 8648 #15 Ace-Thred pressure tube equipped with
bushing and plunger valve containing vinyl chloride (5 mL, 0.072
mol), solvent (o-DCB, 10 mL), initiator
(1,2,4,5-tetrakis(bromomethylmethyl)benzene, 16 mg, 0.035 mmol),
catalyst (copper, 18 mg, 0.28 mmol) and ligand (bpy, 87 mg, 0.56
mmd) was degassed by three freeze-vacuum pump-thaw cycles and
filled with argon. The reaction mixture was slowly heated to
130.degree. C. in an oil bath. After 20 hours, the tube was slowly
cooled and excess vinyl chloride was allowed to boil off. Methylene
chloride (10 mL) was added and the solution was precipitated into
methanol, filtered and dried to yield 0.3 g (7%) of PVC, Mn=23,700,
Mw/Mn=1.58.
Table 4, Example 61
A 50 mL Ace Glass 8648 #15 Ace-Thred pressure tube equipped with
bushing and plunger valve containing vinyl chloride (5 mL, 0.072
mol), solvent (o-DCB, 10 mL), initiator (propanoic acid,
2-bromo-2-methyl-(1-methylethylidene)-di-4,1-phenylene ester 150
mg, 0.28 mmol), catalyst (copper, 72 mg, 1.12 mmol) and ligand
(bpy, 350 mg, 2.2 mmol) was degassed by three freeze-vacuum
pump-thaw cycles and filled with argon. The reaction mixture was
slowly heated to 90.degree. C. in an oil bath. After 22 hours, the
tube was slowly cooled and excess vinyl chloride was allowed to
boil off. Methylene chloride (10 mL) was added and the solution was
precipitated into methanol, filtered and dried to yield 1.7 g (35%)
of PVC, Mn=6,300, Mw/Mn=1.45.
Table 4, Example 65
A 50 mL Ace Glass 8648 #15 Ace-Thred pressure tube equipped with
bushing and plunger valve containing vinyl chloride (5 mL, 0.072
mol), solvent (o-DCB, 10 mL), initiator (propanoic acid,
2-bromo-2-methyl-4,4'-biphenylene ester 135 mg, 0.28 mmol),
catalyst (copper, 72 mg, 1.12 mmol) and ligand (bpy, 350 mg, 2.2
mmol) was degassed by three freeze-vacuum pump-thaw cycles and
filled with argon. The reaction mixture was slowly heated to
130.degree. C. in an oil bath. After 22 hours, the tube was slowly
cooled and excess vinyl chloride was allowed to boil off. Methylene
chloride (10 mL) was added and the solution was precipitated into
methanol, filtered and dried to yield 1.35 g (31%) of PVC,
Mn=5,600, Mw/Mn=1.48.
Table 4, Example 67
A 50 mL Ace Glass 8648 #15 Ace-Thred pressure tube equipped with
bushing and plunger valve containing vinyl chloride (5 mL, 0.072
mol), solvent (o-DCB, 10 mL), initiator (1-chloro-1-bromoethane 103
mg, 0.72 mmol), catalyst (copper, 92 mg, 1.44 mmol) and ligand
(bpy, 450 mg, 2.9 mmol) was degassed by three freeze-vacuum
pump-thaw cycles and filled with argon. The reaction mixture was
slowly heated to 130.degree. C. in an oil bath. After 20 hours, the
tube was slowly cooled and excess vinyl chloride was allowed to
boil off. Methylene chloride (10 mL) was added and the solution was
precipitated into methanol, filtered and dried to yield 1.79 g
(40%) of PVC, Mn=6,000, Mw/Mn=2.30.
Table 4, Example 70
A 50 mL Ace Glass 8648 #15 Ace-Thred pressure tube equipped with
bushing and plunger valve containing vinyl chloride (5 mL, 0.072
mol), solvent (o-DCB, 10 mL), initiator
(.alpha.,.alpha.'-dibromo-p-xylene 33 mg, 0.28 mmol), catalyst
(copper, 72 mg, 1.12 mmol) and ligand (bpy, 350 mg, 2.2 mmol) was
degassed by three freeze-vacuum pump-thaw cycles and filled with
argon. The reaction mixture was slowly heated to 130.degree. C. in
an oil bath. After 20 hours, the tube was slowly cooled and excess
vinyl chloride was allowed to boil off. Methylene chloride (10 mL)
was added and the solution was precipitated into methanol, filtered
and dried to yield 1.95 g (43%) of PVC, Mn=11,000, Mw/Mn=1.63.
Table 4, Example 72
A 50 mL Ace Glass 8648 #15 Ace-Thred pressure tube equipped with
bushing and plunger valve containing vinyl chloride (5 mL, 0.072
mol), solvent (o-DCB, 10 mL), initiator (propanoic acid,
2-iodo-2-methyl-4,4'-biphenylene ester 162 mg, 0.28 mmol), catalyst
(copper, 72 mg, 1.12 mmol) and ligand (bpy, 350 mg, 2.2 mmol) was
degassed by three freeze-vacuum pump-thaw cycles and filled with
argon. The reaction mixture was slowly heated to 130.degree. C. in
an oil bath. After 20 hours, the tube was slowly cooled and excess
vinyl chloride was allowed to boil off. Methylene chloride (10 mL)
was added and the solution was precipitated into methanol, filtered
and dried to yield 1.75 g (38%) of PVC, Mn=6,700, Mw/Mn=1.47.
Table 4, Example 74
A 50 mL Ace Glass 8648 #15 Ace-Thred pressure tube equipped with
bushing and plunger valve containing vinyl chloride (5 mL, 0.072
mol), solvent (o-DCB, 10 mL), initiator
(1,1,1-tris(4-(2-iodo-2-methylpropanoylphenyl))ethane 167 mg, 0.19
mmol), catalyst (copper, 72 mg, 1.12 mmol) and ligand (bpy, 350 mg,
2.2 mmol) was degassed by three freeze-vacuum pump-thaw cycles and
filled with argon. The reaction mixture was slowly heated to
130.degree. C. in an oil bath. After 70 hours, the tube was slowly
cooled and excess vinyl chloride was allowed to boil off. Methylene
chloride (10 mL) was added and the solution was precipitated into
methanol, filtered and dried to yield 1.7 g (37%) of PVC, Mn=8,600,
Mw/Mn=1.67.
Table 4, Example 75
A 50 mL Ace Glass 8648 #15 Ace-Thred pressure tube equipped with
bushing and plunger valve containing vinyl chloride (5 mL, 0.072
mol), solvent (o-DCB, 10 mL), initiator (iodoperflorodecane 180 mg,
0.28 mmol), catalyst (copper, 25 mg, 0.56 mmol) and ligand (bpy,
175 mg, 1.1 mmol) was degassed by three freeze-vacuum pump-thaw
cycles and filled with argon. The reaction mixture was slowly
heated to 130.degree. C. in an oil bath. After 20 hours, the tube
was slowly cooled and excess vinyl chloride was allowed to boil
off. Methylene chloride (10 mL) was added and the solution was
precipitated into methanol, filtered and dried to yield 1.2 g (26%)
of PVC, Mn=5,800, Mw/Mn=1.64.
Table 4, Example 78
A 50 mL Ace Glass 8648 #15 Ace-Thred pressure tube equipped with
bushing and plunger valve containing vinyl chloride (5 mL, 0.072
mol), solvent (o-DCB, 10 mL), initiator (allyl iodide 47 mg, 0.28
mmol), catalyst (copper, 36 mg, 0.56 mmol) and ligand (bpy, 175 mg,
1.1 mmol) was degassed by three freeze-vacuum pump-thaw cycles and
filled with argon. The reaction mixture was slowly heated to
130.degree. C. in an oil bath. After 20 hours, the tube was slowly
cooled and excess vinyl chloride was allowed to boil off. Methylene
chloride (10 mL) was added and the solution was precipitated into
methanol, filtered and dried to yield 1 g (22%) of PVC, Mn=6,800,
Mw/Mn=1.72.
Table 4, Example 80
A 50 mL Ace Glass 8648 #15 Ace-Thred pressure tube equipped with
bushing and plunger valve containing vinyl chloride (5 mL, 0.072
mol), solvent (o-DCB, 10 mL), initiator (iodoform, CHI.sub.3, 567
mg, 1.44 mmol), catalyst (copper, 138 mg, 2.11 mmol) and ligand
(bpy, 675 mg, 4.3 mmol) was degassed by three freeze-vacuum
pump-thaw cycles and filled with argon. The reaction mixture was
slowly heated to 130.degree. C. in an oil bath. After 20 hours, the
tube was slowly cooled and excess vinyl chloride was allowed to
boil off. Methylene chloride (10 mL) was added and the solution was
precipitated into methanol, filtered and dried to yield 0.36 g (8%)
of PVC, Mn=3.300, Mw/Mn=1.25.
Table 4, Example 80
A 50 mL Ace Glass 8648 #15 Ace-Thred pressure tube equipped with
bushing and plunger valve containing vinyl chloride (5 mL, 0.072
mol), solvent (o-DCB, 10 mL), initiator (iodoform, CHI.sub.3, 190
mg, 0.48 mmol), catalyst (copper, 184 mg, 2.8 mmol) and ligand
(bpy, 900 mg, 5.8 mmol) was degassed by three freeze-vacuum
pump-thaw cycles and filled with argon. The reaction mixture was
slowly heated to 130.degree. C. in an oil bath. After 20 hours, the
tube was slowly cooled and excess vinyl chloride was allowed to
boil off. Methylene chloride (10 mL) was added and the solution was
precipitated into methanol, filtered and dried to yield 1.45 g
(33%) of PVC, Mn=6.100, Mw/Mn=1.65.
Table 4, Example 86
A 50 mL Ace Glass 8648 #15 Ace-Thred pressure tube equipped with
bushing and plunger valve containing vinyl chloride (5 mL, 0.072
mol), solvent (o-DCB, 10 mL), initiator (iodoform, CHI.sub.3, 18.4
mg, 0.05 mmol), catalyst (copper, 36 mg, 0.56 mmol) and ligand
(bpy, 175 mg, 1.12 mmol) was degassed by three freeze-vacuum
pump-thaw cycles and filled with argon. The reaction mixture was
slowly heated to 130.degree. C. in an oil bath. After 20 hours, the
tube was slowly cooled and excess vinyl chloride was allowed to
boil off. Methylene chloride (10 mL) was added and the solution was
precipitated into methanol, filtered and dried to yield 0.5 g (11%)
of PVC, Mn=30,000, Mw/Mn 1.63.
Table 4, Example 88
A 50 mL Ace Glass 8648 #15 Ace-Thred pressure tube equipped with
bushing and plunger valve containing vinyl chloride (5 mL, 0.072
mol), solvent (o-DCB, 10 mL), initiator (iodoform, CHI.sub.3, 9.2
mg, 0.02 mmol), catalyst (copper, 18 mg, 0.28 mmol) and ligand
(bpy, 87 mg, 0.56 mmol) was degassed by three freeze-vacuum
pump-thaw cycles and filled with argon. The reaction mixture was
slowly heated to 130.degree. C. in an oil bath. After 20 hours, the
tube was slowly cooled and excess vinyl chloride was allowed to
boil off. Methylene chloride (10 mL) was added and the solution was
precipitated into methanol, filtered and dried to yield 0.34 g (8%)
of PVC, Mn=45,000, Mw/Mn=1.59.
Table 4, Example 89
A 50 mL Ace Glass 8648 #15 Ace-Thred pressure tube equipped with
bushing and plunger valve containing vinyl chloride (5 mL, 0.072
mol), solvent (o-DCB, 10 mL), initiator (iodoform, CHI.sub.3, 190
mg, 0.48 mmol), catalyst (copper, 23 mg, 0.36 mmol) and ligand
(tris(2-aminoethyl)amine (TREN), 52 mg, 0.36 mmol) was degassed by
three freeze-vacuum pump-thaw cycles and filled with argon. The
reaction mixture was slowly heated to 130.degree. C. in an oil
bath. After 20 hours, the tube was slowly cooled and excess vinyl
chloride was allowed to boil off. Methylene chloride (10 mL) was
added and the solution was precipitated into methanol, filtered and
dried to yield 0.45 g (10%) of PVC, Mn=5,000, Mw/Mn=1.58.
Table 4, Example 91
A 50 mL Ace Glass 8648 #15 Ace-Thred pressure tube equipped with
bushing and plunger valve containing vinyl chloride (5 mL, 0.072
mol), solvent (o-DCB, 10 mL), initiator (carbon tetraiodide,
Cl.sub.4, 37 mg, 0.07 mmol), catalyst (copper, 37 mg, 0.57 mmol)
and ligand (bpy, 180 mg, 1.15 mmol) was degassed by three
freeze-vacuum pump-thaw cycles and filled with argon. The reaction
mixture was slowly heated to 130.degree. C. in an oil bath. After
20 hours, the tube was slowly cooled and excess vinyl chloride was
allowed to boil off. Methylene chloride (10 mL) was added and the
solution was precipitated into methanol, filtered and dried to
yield 0.29 g (7%) of PVC, Mn=17,400, Mw/Mn=1.52.
Table 4, Example 97
A 50 mL Ace Glass 8648 #15 Ace-Thred pressure tube equipped with
bushing and plunger valve containing vinyl chloride (5 mL, 0.072
mol), initiator (1-iodo-1-chloroethane, 137 mg, 0.72 mmol),
catalyst (copper, 92 mg, 1.44 mmol) and ligand (bpy, 450 mg, 2.88
mmol) was degassed by three freeze-vacuum pump-thaw cycles and
filled with argon. The reaction mixture was slowly heated to
60.degree. C. in an oil bath. After 20 hours, the tube was slowly
cooled and excess vinyl chloride was allowed to boil off. Methylene
chloride (10 mL) was added and the solution was precipitated into
methanol, filtered and dried to yield 0.66 g (15%) of PVC,
Mn=5,200, Mw/Mn=1.78.
Table 4, Example 98
A 50 mL Ace Glass 8648 #15 Ace-Thred pressure tube equipped with
bushing and plunger valve containing vinyl chloride (5 mL, 0.072
mol), solvent (o-DCB, 2.5 mL) initiator (1-iodo-1-chloroethane, 137
mg, 0.72 mmol), catalyst (copper, 92 mg, 1.44 mmol) and ligand
(bpy, 450 mg, 2.88 mmol) was degassed by three freeze-vacuum
pump-thaw cycles and filled with argon. The reaction mixture was
slowly heated to 60.degree. C. in an oil bath. After 20 hours, the
tube was slowly cooled and excess vinyl chloride was allowed to
boil off. Methylene chloride (10 mL) was added and the solution was
precipitated into methanol, filtered and dried to yield 1 g (22%)
of PVC, Mn=5,600, Mw/Mn=1.77.
Table 4, Example 99
A 50 mL Ace Glass 8648 #15 Ace-Thred pressure tube equipped with
bushing and plunger valve containing vinyl chloride (5 mL, 0.072
mol), solvent (o-DCB, 5 mL) initiator (1-iodo-1-chloroethane, 137
mg, 0.72 mmol), catalyst (copper, 92 mg, 1.44 mmol) and ligand
(bpy, 450 mg, 2.88 mmol) was degassed by three freeze-vacuum
pump-thaw cycles and filled with argon. The reaction mixture was
slowly heated to 60.degree. C. in an oil bath. After 20 hours, the
tube was slowly cooled and excess vinyl chloride was allowed to
boil off. Methylene chloride (10 mL) was added and the solution was
precipitated into methanol, filtered and dried to yield 1.17 g
(26%) of PVC, Mn=6,200, Mw/Mn=1.78.
Table 4, Example 100
A 50 mL Ace Glass 8648 #15 Ace-Thred pressure tube equipped with
bushing and plunger valve containing vinyl chloride (5 mL, 0.072
mol), solvent (o-DCB, 5 mL) initiator (1-iodo-1-chloroethane, 137
mg, 0.72 mmol), catalyst (copper, 92 mg, 1.44 mmol) and ligand
(bpy, 450 mg, 2.88 mmol) was degassed by three freeze-vacuum
pump-thaw cycles and filled with argon. The reaction mixture was
slowly heated to 60.degree. C. in an oil bath. After 20 hours, the
tube was slowly cooled and excess vinyl chloride was allowed to
boil off. Methylene chloride (10 mL) was added and the solution was
precipitated into methanol, filtered and dried to yield 0.63 g
(14%) of PVC, Mn=6,500, Mw/Mn=1.69.
Table 4, Example 101
A 50 mL Ace Glass 8648 #15 Ace-Thred pressure tube equipped with
bushing and plunger valve containing vinyl chloride (5 mL, 0.072
mol), initiator (1-iodo-1-chloroethane, 137 mg, 0.72 mmol),
catalyst (copper, 92 mg, 1.44 mmol) and ligand (bpy, 450 mg, 2.88
mmol) was degassed by three freeze-vacuum pump-thaw cycles and
filled with argon. The reaction mixture was slowly heated to
90.degree. C. in an oil bath. After 20 hours, the tube was slowly
cooled and excess vinyl chloride was allowed to boil off. Methylene
chloride (10 mL) was added and the solution was precipitated into
methanol, filtered and dried to yield 0.81 g (18%) of PVC,
Mn=5,400, Mw/Mn=1.87.
Table 4, Example 104
A 50 mL Ace Glass 8648 #15 Ace-Thred pressure tube equipped with
bushing and plunger valve containing vinyl chloride (5 mL, 0.072
mol), solvent (o-DCB, 5 mL) initiator (1-iodo-1-chloroethane, 137
mg, 0.72 mmol), catalyst (copper, 92 mg, 1.44 mmol) and ligand
(bpy, 450 mg, 2.88 mmol) was degassed by three freeze-vacuum
pump-thaw cycles and filled with argon. The reaction mixture was
slowly heated to 90.degree. C. in an oil bath. After 20 hours, the
tube was slowly cooled and excess vinyl chloride was allowed to
boil off. Methylene chloride (10 mL) was added and the solution was
precipitated into methanol, filtered and dried to yield 0.63 g
(14%) of PVC, Mn=6,500, Mw/Mn=1.69.
Table 4, Example 107
A 50 mL Ace Glass 8648 #15 Ace-Thred pressure tube equipped with
bushing and plunger valve containing vinyl chloride (5 mL, 0.072
mol), solvent (o-DCB, 5 mL) initiator (1-iodo-1-chloroethane, 137
mg, 0.72 mmol), catalyst (copper, 92 mg, 1.44 mmol) and ligand
(bpy, 450 mg, 2.88 mmol) was degassed by three freeze-vacuum
pump-thaw cycles and filled with argon. The reaction mixture was
slowly heated to 130.degree. C. in an oil bath. After 20 hours, the
tube was slowly cooled and excess vinyl chloride was allowed to
boil off. Methylene chloride (10 mL) was added and the solution was
precipitated into methanol, filtered and dried to yield 1.95 g
(43%) of PVC, Mn=7,100, Mw/Mn=1.65.
Table 4, Example 109
A 50 mL Ace Glass 8648 #15 Ace-Thred pressure tube equipped with
bushing and plunger valve containing vinyl chloride (5 mL, 0.072
mol), deionized water 8 mL), initiator (1-iodo-1-chloroethane, 137
mg, 0.72 mmol), catalyst (copper, 92 mg, 1.44 mmol), ligand (bpy,
450 mg, 2.88 mmol) and surfactant
(CH.sub.3--(CH.sub.2).sub.11--SO.sub.3Na, (NaDDS, sodium
dodecylsulfate), 21 mg, 0.072 mmol) was degassed by three
freeze-vacuum pump-thaw cycles and filled with argon. The reaction
mixture was slowly heated to 90.degree. C. in an oil bath. After 20
hours, the tube was slowly cooled and excess vinyl chloride was
allowed to boil off. Methylene chloride (10 mL) was added and the
mixture was precipitated into methanol, filtered and dried to yield
2.38 g (53%) of PVC, Mn=10,600, Mw/Mn=1.65.
Table 4, Example 110
A 50 mL Ace Glass 8648 #15 Ace-Thred pressure tube equipped with
bushing and plunger valve containing vinyl chloride (5 mL, 0.072
mol), deionized water 8 mL), initiator (1-iodo-1-chloroethane, 137
mg, 0.72 mmol), catalyst (copper, 92 mg, 1.44 mmol), ligand (bpy,
450 mg, 2.88 mmol) and surfactant
(CH.sub.3--(CH.sub.2).sub.11--SO.sub.3Na, (NaDDS, sodium
dodecylsulfate), 104 mg, 0.36 mmol) was degassed by three
freeze-vacuum pump-thaw cycles and filled with argon. The reaction
mixture was slowly heated to 90.degree. C. in an oil bath. After 20
hours, the tube was slowly cooled and excess vinyl chloride was
allowed to boil off. Methylene chloride (10 mL) was added and the
mixture was precipitated into methanol, filtered and dried to yield
2.11 g (47%) of PVC, Mn=8,500, Mw/Mn=1.69.
Table 4, Example 111
A 50 mL Ace Glass 8648 #15 Ace-Thred pressure tube equipped with
bushing and plunger valve containing vinyl chloride (5 mL, 0.072
mol), deionized water 8 mL), initiator (1-iodo-1-chloroethane, 137
mg, 0.72 mmol), catalyst (copper, 92 mg, 1.44 mmol), ligand (bpy,
450 mg, 2.88 mmol) and surfactant
(CH.sub.3--(CH.sub.2).sub.11--SO.sub.3Na, (NaDDS, sodium
dodecylsulfate), 208 mg, 0.72 mmol) was degassed by three
freeze-vacuum pump-thaw cycles and filled with argon. The reaction
mixture was slowly heated to 90.degree. C. in an oil bath. After 20
hours, the tube was slowly cooled and excess vinyl chloride was
allowed to boil off. Methylene chloride (10 mL) was added and the
mixture was precipitated into methanol, filtered and dried to yield
1.84 g (41%) of PVC, Mn=7,000, Mw/Mn=1.75.
Table 4, Example 112
A 50 mL Ace Glass 8648 #15 Ace-Thred pressure tube equipped with
bushing and plunger valve containing vinyl chloride (5 mL, 0.072
mol), deionized water 8 mL), initiator (1-iodo-1-chloroethane, 137
mg, 0.72 mmol), catalyst (copper, 92 mg, 1.44 mmol), ligand (bpy,
450 mg, 2.88 mmol) and surfactant
(CH.sub.3--(CH.sub.2).sub.11--SO.sub.3Na, (NaDDS, sodium
dodecylsulfate), 416 mg, 1.44 mmol) was degassed by three
freeze-vacuum pump-thaw cycles and filled with argon. The reaction
mixture was slowly heated to 90.degree. C. in an oil bath. After 20
hours, the tube was slowly cooled and excess vinyl chloride was
allowed to boil off. Methylene chloride (10 mL) was added and the
mixture was precipitated into methanol, filtered and dried to yield
1.93 g (43%) of PVC, Mn=7,500, Mw/Mn=1.76.
Table 4, Example 112
A 50 mL Ace Glass 8648 #15 Ace-Thred pressure tube equipped with
bushing and plunger valve containing vinyl chloride (5 mL, 0.072
mol), deionized water 8 mL), initiator (1-iodo-1-chloroethane, 137
mg, 0.72 mmol), catalyst (copper, 92 mg, 1.44 mmol), ligand (bpy,
450 mg, 2.88 mmol) and surfactant
(CH.sub.3--(CH.sub.2).sub.11--SO.sub.3Na, (NaDDS, sodium
dodecylsulfate), 416 mg, 1.44 mmol) was degassed by three
freeze-vacuum pump-thaw cycles and filled with argon. The reaction
mixture was slowly heated to 90.degree. C. in an oil bath. After 20
hours, the tube was slowly cooled and excess vinyl chloride was
allowed to boil off. Methylene chloride (10 mL) was added and the
mixture was precipitated into methanol, filtered and dried to yield
1.93 g (43%) of PVC, Mn=7,500, Mw/Mn=1.76.
Table 4, Example 113
A 50 mL Ace Glass 8648 #15 Ace-Thred pressure tube equipped with
bushing and plunger valve containing vinyl chloride (5 mL, 0.072
mol), deionized water 8 mL), initiator (1-iodo-1-chloroethane, 137
mg, 0.72 mmol), catalyst (copper, 92 mg, 1.44 mmol), ligand (bpy,
450 mg, 2.88 mmol) and surfactant
(CH.sub.3--(CH.sub.2).sub.11--SO.sub.3Na, (NaDDS, sodium
dodecylsulfate), 830 mg, 2.88 mmol) was degassed by three
freeze-vacuum pump-thaw cycles and filled with argon. The reaction
mixture was slowly heated to 90.degree. C. in an oil bath. After 20
hours, the tube was slowly cooled and excess vinyl chloride was
allowed to boil off. Methylene chloride (10 mL) was added and the
mixture was precipitated into methanol, filtered and dried to yield
2.02 g (45%) of PVC, Mn=7,300, Mw/Mn=1.72.
Table 4, Example 114
A 50 mL Ace Glass 8648 #15 Ace-Thred pressure tube equipped with
bushing and plunger valve containing vinyl chloride (5 mL, 0.072
mol), deionized water 8 mL), initiator (1-iodo-1-chloroethane, 137
mg, 0.72 mmol), catalyst (copper, 92 mg, 1.44 mmol), ligand (bpy,
450 mg, 2.88 mmol) and surfactant
(CH.sub.3--(CH.sub.2).sub.11--SO.sub.3Na, NaDDS, sodium
dodecylsulfate), 104 mg, 0.36 mmol) was degassed by three
freeze-vacuum pump-thaw cycles and filled with argon. The reaction
mixture was slowly heated to 90.degree. C. in an oil bath. After 1
hour, the tube was slowly cooled and excess vinyl chloride was
allowed to boil off. Methylene chloride (10 mL) was added and the
mixture was precipitated into methanol, filtered and dried to yield
1.35 g (30%) of PVC, Mn=4,700, Mw/Mn=1.67.
Table 4, Example 115
A 50 mL Ace Glass 8648 #15 Ace-Thred pressure tube equipped with
bushing and plunger valve containing vinyl chloride (5 mL, 0.072
mol), deionized water 8 mL), initiator (1-iodo-1-chloroethane, 137
mg, 0.72 mmol), catalyst (copper, 92 mg, 1.44 mmol), ligand (bpy,
450 mg, 2.88 mmol) and surfactant
(CH.sub.3--(CH.sub.2).sub.11--SO.sub.3Na, NaDDS, sodium
dodecylsulfate), 104 mg, 0.36 mmol) was degassed by three
freeze-vacuum pump-thaw cycles and filled with argon. The reaction
mixture was slowly heated to 90.degree. C. in an oil bath. After 2
hours, the tube was slowly cooled and excess vinyl chloride was
allowed to boil off. Methylene chloride (10 mL) was added and the
mixture was precipitated into methanol, filtered and dried to yield
1.49 g (34%) of PVC, Mn=6,200, Mw/Mn=1.71.
Table 4, Example 116
A 50 mL Ace Glass 8648 #15 Ace-Thred pressure tube equipped with
bushing and plunger valve containing vinyl chloride (5 mL, 0.072
mol), deionized water 8 mL), initiator (1-iodo-1-chloroethane, 137
mg, 0.72 mmol), catalyst (copper, 92 mg, 1.44 mmol), ligand (bpy,
450 mg, 2.88 mmol) and surfactant
(CH.sub.3--(CH.sub.2).sub.11--SO.sub.3Na, NaDDS, sodium
dodecylsulfate), 104 mg, 0.36 mmol) was degassed by three
freeze-vacuum pump-thaw cycles and filled with argon. The reaction
mixture was slowly heated to 90.degree. C. in an oil bath. After 4
hours, the tube was slowly cooled and excess vinyl chloride was
allowed to boil off. Methylene chloride (10 mL) was added and the
mixture was precipitated into methanol, filtered and dried to yield
1.98 g (44%) of PVC, Mn=7,100, Mw/Mn=1.76.
Table 4, Example 117
A 50 mL Ace Glass 8648 #15 Ace-Thred pressure tube equipped with
bushing and plunger valve containing vinyl chloride (5 mL, 0.072
mol), deionized water 8 mL), initiator (1-iodo-1-chloroethane, 137
mg, 0.72 mmol), catalyst (copper, 92 mg, 1.44 mmol), ligand (bpy,
450 mg, 2.88 mmol) and surfactant
(CH.sub.3--(CH.sub.2).sub.11--SO.sub.3Na, NaDDS, sodium
dodecylsulfate), 104 mg, 0.36 mmol) was degassed by three
freeze-vacuum pump-thaw cycles and filled with argon. The reaction
mixture was slowly heated to 90.degree. C. in an oil bath. After 8
hours, the tube was slowly cooled and excess vinyl chloride was
allowed to boil off. Methylene chloride (10 mL) was added and the
mixture was precipitated into methanol, filtered and dried to yield
1.98 g (44%) of PVC, Mn=8,500, Mw/Mn=1.73.
Table 4, Example 118
A 50 mL Ace Glass 8648 #15 Ace-Thred pressure tube equipped with
bushing and plunger valve containing vinyl chloride (5 mL, 0.072
mol), solvent (o-DCB, 10 mL), initiator
(.alpha.,.alpha.'-diiodo-p-xylene, 25 mg, 0.07 mmol), catalyst
(copper, 36 mg, 0.56 mmol) and ligand (bpy, 175 mg, 1.12 mmol) was
degassed by three freeze-vacuum pump-thaw cycles and filled with
argon. The reaction mixture was slowly heated to 130.degree. C. in
an oil bath. After 20 hours, the tube was slowly cooled and excess
vinyl chloride was allowed to boil off. Methylene chloride (10 mL)
was added and the solution was precipitated into methanol, filtered
and dried to yield 1.57 g (35%) of PVC, Mn=7,900, Mw/Mn=1.61.
Table 4, Example 119
A 50 mL Ace Glass 8648 #15 Ace-Thred pressure tube equipped with
bushing and plunger valve containing vinyl chloride (5 mL, 0.072
mol), solvent (o-DCB, 10 mL), initiator
(.alpha.,.alpha.'-diiodo-p-xylene, 200 mg, 0.56 mmol), catalyst
(copper, 143 mg, 2.24 mmol) and ligand (bpy, 700 mg, 4.48 mmol) was
degassed by three freeze-vacuum pump-thaw cycles and filled with
argon. The reaction mixture was slowly heated to 130.degree. C. in
an oil bath. After 20 hours, the tube was slowly cooled and excess
vinyl chloride was allowed to boil off. Methylene chloride (10 mL)
was added and the solution was precipitated into methanol, filtered
and dried to yield 1.48 g (31%) of PVC, Mn=10,300, Mw/Mn=1.58.
Table 4, Example 120
A 50 mL Ace Glass 8648 #15 Ace-Thred pressure tube equipped with
bushing and plunger valve containing vinyl chloride (5 mL, 0.072
mol), solvent (ethylene carbonate, 13.2 g, 10 mL), initiator
(.alpha.,.alpha.'-diiodo-p-xylene, 100 mg, 0.28 mmol), catalyst
(copper, 72 mg, 1.12 mmol) and ligand (bpy, 250 mg, 2.21 mmol) was
degassed by three freeze-vacuum pump-thaw cycles and filled with
argon. The reaction mixture was slowly heated to 130.degree. C. in
an oil bath. After 20 hours, the tube was slowly cooled and excess
vinyl chloride was allowed to boil off. Methylene chloride (10 mL)
was added and the solution was precipitated into methanol, filtered
and dried to yield 0.85 g (19%) of PVC, Mn=8,400, Mw/Mn=1.56.
Table 4, Example 121
A 50 mL Ace Glass 8648 #15 Ace-Thred pressure tube equipped with
bushing and plunger valve containing vinyl chloride (5 mL, 0.072
mol), solvent (o-DCB, 10 mL), initiator
(.alpha.,.alpha.'-diiodo-p-xylene, 50 mg, 0.14 mmol), catalyst
(copper, 36 mg, 0.56.mmol) and ligand
(tris[2-(dimethylamino)ethyl]amine (Me.sub.6-TREN) 128 mg, 0.56
mmol) was degassed by three freeze-vacuum pump-thaw cycles and
filled with argon. The reaction mixture was slowly heated to
130.degree. C. in an oil bath. After 20 hours, the tube was slowly
cooled and excess vinyl chloride was allowed to boil off. Methylene
chloride (10 mL) was added and the solution was precipitated into
methanol, filtered and dried to yield 0.63 g (19%) of PVC,
Mn=3,000, Mw/Mn=1.80.
Table 4, Example 122
A 50 mL Ace Glass 8648 #15 Ace-Thred pressure tube equipped with
bushing and plunger valve containing vinyl chloride (5 mL, 0.072
mol), solvent (o-DCB, 10 mL), initiator
(.alpha.,.alpha.'-diiodo-p-xylene, 50 mg, 0.14 mmol), catalyst
(copper, 36 mg, 0.56 mmol) and (tris(2-aminoethyl)amine (TREN), 164
mg, 1.12 mmol) was degassed by three freeze-vacuum pump-thaw cycles
and filled with argon. The reaction mixture was slowly heated to
130.degree. C. in an oil bath. After 20 hours, the tube was slowly
cooled and excess vinyl chloride was allowed to boil off. Methylene
chloride (10 mL) was added and the mixture was precipitated into
methanol, filtered and dried to yield 1.66 g (37%) of PVC.
Table 4, Example 123
A 50 mL Ace Glass 8648 #15 Ace-Thred pressure tube equipped with
bushing and plunger valve containing vinyl chloride (5 mL, 0.072
mol), solvent (dimethylsulfoxide, DMSO, 10 mL), initiator
(.alpha.,.alpha.'-diiodo-p-xylene, 50 mg, 0.14 mmol), catalyst
(copper, 36 mg, 0.56 mmol) and ligand (bpy, 175 mg, 1.12 mmol) was
degassed by three freeze-vacuum pump-thaw cycles and filled with
argon. The reaction mixture was slowly heated to 130.degree. C. in
an oil bath. After 20 hours, the tube was slowly cooled and excess
vinyl chloride was allowed to boil off. Methylene chloride (10 mL)
was added and the solution was precipitated into methanol, filtered
and dried to yield 0.22 g (5%) of PVC, Mn=3,100, Mw/Mn=2.05.
Table 4, Example 124
A 50 mL Ace Glass 8648 #15 Ace-Thred pressure tube equipped with
bushing and plunger valve containing vinyl chloride (5 mL, 0.072
mol), solvent (dimethylformamide, DMF, 10 mL), initiator
(.alpha.,.alpha.'-diiodo-p-xylene, 100 mg, 0.28 mmol), catalyst
(copper, 72 mg, 1.12 mmol) and ligand (bpy, 350 mg, 2.24 mmol) was
degassed by three freeze-vacuum pump-thaw cycles and filled with
argon. The reaction mixture was slowly heated to 130.degree. C. in
an oil bath. After 22 hours, the tube was slowly cooled and excess
vinyl chloride was allowed to boil off. Methylene chloride (10 mL)
was added and the solution was precipitated into methanol, filtered
and dried to yield 0.8 g (18%) of PVC, Mn=6,100, Mw/Mn=2.02.
Table 4, Example 125
A 50 mL Ace Glass 8648 #15 Ace-Thred pressure tube equipped with
bushing and plunger valve containing vinyl chloride (5 mL, 0.072
mol), solvent (o-DCB, 10 mL), initiator
(.alpha.,.alpha.'-diiodo-p-xylene, 100 mg, 0.28 mmol), catalyst
(copper, 72 mg, 1.12 mmol) and ligand (bpy, 350 mg, 2.24 mmol) was
degassed by three freeze-vacuum pump-thaw cycles and filled with
argon. The reaction mixture was slowly heated to 130.degree. C. in
an oil bath. After 1 hour, the tube was slowly cooled and excess
vinyl chloride was allowed to boil off. Methylene chloride (10 mL)
was added and the solution was precipitated into methanol, filtered
and dried to yield 0.07 g (1.5%) of PVC, Mn=1,100, Mw/Mn=1.98.
Table 4, Example 126
A 50 mL Ace Glass 8648 #15 Ace-Thred pressure tube equipped with
bushing and plunger valve containing vinyl chloride (5 mL, 0.072
mol), solvent (o-DCB, 10 mL), initiator
(.alpha.,.alpha.'-diiodo-p-xylene, 100 mg, 0.28 mmol), catalyst
(copper, 72 mg, 1.12 mmol) and ligand (bpy, 350 mg, 2.24 mmol) was
degassed by three freeze-vacuum pump-thaw cycles and filled with
argon. The reaction mixture was slowly heated to 130.degree. C. in
an oil bath. After 2 hours, the tube was slowly cooled and excess
vinyl chloride was allowed to boil off. Methylene chloride (10 mL)
was added and the solution was precipitated into methanol, filtered
and dried to yield 0.3 g (6.6%) of PVC, Mn=4,100, Mw/Mn=1.68.
Table 4, Example 127
A 50 mL Ace Glass 8648 #15 Ace-Thred pressure tube equipped with
bushing and plunger valve containing vinyl chloride (5 mL, 0.072
mol), solvent (o-DCB, 10 mL), initiator
(.alpha.,.alpha.'-diiodo-p-xylene, 100 mg, 0.28 mmol), catalyst
(copper, 72 mg, 1.12 mmol) and ligand (bpy, 350 mg, 2.24 mmol) was
degassed by three freeze-vacuum pump-thaw cycles and filled with
argon. The reaction mixture was slowly heated to 130.degree. C. in
an oil bath. After 4 hours, the tube was slowly cooled and excess
vinyl chloride was allowed to boil off. Methylene chloride (10 mL)
was added and the solution was precipitated into methanol, filtered
and dried to yield 0.46 g (11%) of PVC, Mn=7,600, Mw/Mn=1.48.
Table 4, Example 128
A 50 mL Ace Glass 8648 #15 Ace-Thred pressure tube equipped with
bushing and plunger valve containing vinyl chloride (5 mL, 0.072
mol), solvent (o-DCB, 10 mL), initiator
(.alpha.,.alpha.'-diiodo-p-xylene, 100 mg, 0.28 mmol), catalyst
(copper, 72 mg, 1.12 mmol) and ligand (bpy, 350 mg, 2.24 mmol) was
degassed by three freeze-vacuum pump-thaw cycles and filled with
argon. The reaction mixture was slowly heated to 130.degree. C. in
an oil bath. After 7 hours, the tube was slowly cooled and excess
vinyl chloride was allowed to boil off. Methylene chloride (10 mL)
was added and the solution was precipitated into methanol, filtered
and dried to yield 0.61 g (13.5%) of PVC, Mn=8,300, Mw/Mn=1.46.
Table 4, Example 129
A 50 mL Ace Glass 8648 #15 Ace-Thred pressure tube equipped with
bushing and plunger valve containing vinyl chloride (5 mL, 0.072
mol), solvent (o-DCB, 10 mL), initiator
(.alpha.,.alpha.'-diiodo-p-xylene, 100 mg, 0.28 mmol), catalyst
(copper, 72 mg, 1.12 mmol) and ligand (bpy, 350 mg, 2.24 mmol) was
degassed by three freeze-vacuum pump-thaw cycles and filled with
argon. The reaction mixture was slowly heated to 130.degree. C. in
an oil bath. After 13 hours, the tube was slowly cooled and excess
vinyl chloride was allowed to boil off. Methylene chloride (10 mL)
was added and the solution was precipitated into methanol, filtered
and dried to yield 0.78 g (17.5%) of PVC, Mn=10,400,
Mw/Mn=1.48.
Table 4, Example 130
A 50 mL Ace Glass 8648 #15 Ace-Thred pressure tube equipped with
bushing and plunger valve containing vinyl chloride (5 mL, 0.072
mol), solvent (o-DCB, 10 mL), initiator
(.alpha.,.alpha.'-diiodo-p-xylene, 50 mg, 0.14 mmol), catalyst
(copper, 36 mg, 0.56 mmol) and ligand (bpy, 175 mg, 1.12 mmol) was
degassed by three freeze-vacuum pump-thaw cycles and filled with
argon. The reaction mixture was slowly heated to 130.degree. C. in
an oil bath. After 2 hours, the tube was slowly cooled and excess
vinyl chloride was allowed to boil off. Methylene chloride (10 mL)
was added and the solution was precipitated into methanol, filtered
and dried to yield 0.1 g (2.2%) of PVC, Mn=2.100, Mw/Mn=2.10.
Table 4, Example 131
A 50 mL Ace Glass 8648 #15 Ace-Thred pressure tube equipped with
bushing and plunger valve containing vinyl chloride (5 mL, 0.072
mol), solvent (o-DCB, 10 mL), initiator
(.alpha.,.alpha.'-diiodo-p-xylene, 50 mg, 0.14 mmol), catalyst
(copper, 36 mg, 0.56 mmol) and ligand (bpy, 175 mg, 1.12 mmol) was
degassed by three freeze-vacuum pump-thaw cycles and filled with
argon. The reaction mixture was slowly heated to 130.degree. C. in
an oil bath. After 5 hours, the tube was slowly cooled and excess
vinyl chloride was allowed to boil off. Methylene chloride (10 mL)
was added and the solution was precipitated into methanol, filtered
and dried to yield 0.34 g (7.5%) of PVC, Mn=7,000, Mw/Mn=1.49.
Table 4, Example 132
A 50 mL Ace Glass 8648 #15 Ace-Thred pressure tube equipped with
bushing and plunger valve containing vinyl chloride (5 mL, 0.072
mol), solvent (o-DCB, 10 mL), initiator
(.alpha.,.alpha.'-diiodo-p-xylene, 50 mg, 0.14 mmol), catalyst
(copper, 36 mg, 0.56 mmol) and ligand (bpy, 175 mg, 1.12 mmol) was
degassed by three freeze-vacuum pump-thaw cycles and filled with
argon. The reaction mixture was slowly heated to 130.degree. C. in
an oil bath. After 11 hours, the tube was slowly cooled and excess
vinyl chloride was allowed to boil off. Methylene chloride (10 mL)
was added and the solution was precipitated into methanol, filtered
and dried to yield 0.49 g (11%) of PVC, Mn=11,000, Mw/Mn=1.45.
Table 4, Example 133
A 50 mL Ace Glass 8648 #15 Ace-Thred pressure tube equipped with
bushing and plunger valve containing vinyl chloride (5 mL, 0.072
mol), solvent (o-DCB, 10 mL), initiator
(.alpha.,.alpha.'-diiodo-p-xylene, 50 mg, 0.14 mmol), catalyst
(copper, 36 mg, 0.56 mmol) ligand (bpy, 175 mg, 1.12 mmol) and
additive (Al.sup.iBu.sub.3, 0.26 mL 1M in tolene, 0.26 mmol) was
degassed by three freeze-vacuum pump-thaw cycles and filled with
argon. The reaction mixture was slowly heated to 130.degree. C. in
an oil bath. After 20 hours, the tube was slowly cooled and excess
vinyl chloride was allowed to boil off. Methylene chloride (10 mL)
was added and the solution was precipitated into methanol, filtered
and dried to yield 0.9 g (20%) of PVC, Mn=12,700, Mw/Mn=1.59.
Table 4, Example 134
A 50 mL Ace Glass 8648 #15 Ace-Thred pressure tube equipped with
bushing and plunger valve containing vinyl chloride (5 mL, 0.072
mol), solvent (o-DCB, 10 mL), initiator
(.alpha.,.alpha.'-diiodo-p-xulene, 50 mg, 0.14 mmol), catalyst
(copper, 72 mg, 1.12 mmol) and ligand (bpy, 175 mg, 1.12 mmol) was
degassed by three freeze-vacuum pump-thaw cycles and filled with
argon. The reaction mixture was slowly heated to 130.degree. C. in
an oil bath. After 21 hours, the tube was slowly cooled and excess
vinyl chloride was allowed to boil off. Methylene chloride (10 mL)
was added and the solution was precipitated into methanol, filtered
and dried to yield 0.95 g (21%) of PVC, Mn=29,600, Mw/Mn=1.89.
Table 4, Example 135
A 50 mL Ace Glass 8648 #15 Ace-Thred pressure tube equipped with
bushing and plunger valve containing vinyl chloride (5 mL, 0.072
mol), solvent (o-DCB, 10 mL), initiator
(.alpha.,.alpha.'-diiodo-p-xylene, 50 mg, 0.14 mmol), catalyst
(copper, 144 mg, 2.24 mmol) and ligand (bpy, 175 mg, 1.12 mmol) was
degassed by three freeze-vacuum pump-thaw cycles and filled with
argon. The reaction mixture was slowly heated to 130.degree. C. in
an oil bath. After 21 hours, the tube was slowly cooled and excess
vinyl chloride was allowed to boil off. Methylene chloride (10 mL)
was added and the mixture was precipitated into methanol, filtered
and dried to yield 1.9 g (42%) of PVC.
Table 4, Example 136
A 50 mL Ace Glass 8648 #15 Ace-Thred pressure tube equipped with
bushing and plunger valve containing vinyl chloride (5 mL, 0.072
mol), solvent (o-DCB, 10 mL), initiator
(.alpha.,.alpha.'-diiodo-p-xylene, 25 mg, 0.07 mmol), catalyst
(copper, 18 mg, 0.28 mmol), ligand (bpy, 88 mg, 0.56 mmol) and
additive (2,6-di-.sup.tbutylpyridine, 115 mg, 0.56 mmol) was
degassed by three freeze-vacuum pump-thaw cycles and filled with
argon. The reaction mixture was slowly heated to 130.degree. C. in
an oil bath. After 21 hours, the tube was slowly cooled and excess
vinyl chloride was allowed to boil off. Methylene chloride (10 mL)
was added and the solution was precipitated into methanol, filtered
and dried to yield 0.4 g (9%) of PVC, Mn=29,600, Mw/Mn=1.89.
Table 4, Example 139
A 50 mL Ace Glass 8648 #15 Ace-Thred pressure tube equipped with
bushing and plunger valve containing vinyl chloride (5 mL, 0.072
mol), solvent (o-DCB, 10 mL), initiator
(.alpha.,.alpha.'-dithiocyanato-p-xylene, 62 mg, 0.28 mmol),
catalyst (copper, 72 mg, 1.12 mmol) and ligand (bpy, 350 mg, 2.24
mmol) was degassed by three freeze-vacuum pump-thaw cycles and
filled with argon. The reaction mixture was slowly heated to
130.degree. C. in an oil bath. After 20 hours, the tube was slowly
cooled and excess vinyl chloride was allowed to boil off. Methylene
chloride (10 mL) was added and the solution was precipitated into
methanol, filtered and dried to yield 1.2 g (26%) of PVC,
Mn=11,000, Mw/Mn=3.14.
Table 5, Example 140
A 50 mL Ace Glass 8648 #15 Ace-Thred pressure tube equipped with
bushing and plunger valve containing vinyl chloride (5 mL, 0.072
mol), solvent (xylene, 10 mL), initiator (ethyl 2-bromoisobutyrate,
111 mg, 0.56 mmol), catalyst (aluminium, 20 mg, 0.74 mmol) and
ligand (bpy, 100 mg, 0.64 mmol) was degassed by three freeze-vacuum
pump-thaw cycles and filled with argon. The reaction mixture was
slowly heated to 90.degree. C. in an oil bath. After 17 hours, the
tube was slowly cooled and excess vinyl chloride was allowed to
boil off. Methylene chloride (10 mL) was added and the solution was
precipitated into methanol, filtered and dried to yield 0.31 g (7%)
of PVC, Mn=8,200, Mw/Mn=1.61.
Table 5, Example 141
A 50 mL Ace Glass 8648 #15 Ace-Thred pressure tube equipped with
bushing and plunger valve containing vinyl chloride (5 mL, 0.072
mol), solvent (o-DCB, 10 mL), initiator (ethyl 2-bromoisobutyrate,
111 mg, 0.56 mmol) and catalyst (triisobutylaluminium,
Al.sup.iBu.sub.3, 0.64 mL 1 M in toluene, 0.64 mmol) was degassed
by three freeze-vacuum pump-thaw cycles and filled with argon. The
reaction mixture was slowly heated to 90.degree. C. in an oil bath.
After 19 hours, the tube was slowly cooled and excess vinyl
chloride was allowed to boil off. Methylene chloride (10 mL) was
added and the solution was precipitated into methanol, filtered and
dried to yield 1.35 g (30%) of PVC, Mn=8,200, Mw/Mn=1.61.
Table 5, Example 142
A 50 mL Ace Glass 8648 #15 Ace-Thred pressure tube equipped with
bushing and plunger valve containing vinyl chloride (5 mL, 0.072
mol), solvent (o-DCB, 10 mL), initiator (ethyl 2-bromoisobutyrate,
111 mg, 0.56 mmol), catalyst (cadmium, 76 mg, 0.68 mmol) and ligand
(bpy, 100 mg, 0.64 mmol) was degassed by three freeze-vacuum
pump-thaw cycles and filled with argon. The reaction mixture was
slowly heated to 90.degree. C. in an oil bath. After 22 hours, the
tube was slowly cooled and excess vinyl chloride was allowed to
boil off. Methylene chloride (10 mL) was added and the solution was
precipitated into methanol, filtered and dried to yield 0.6 g (14%)
of PVC, Mn=14,100, Mw/Mn=1.65.
Table 5, Example 143
A 50 mL Ace Glass 8648 #15 Ace-Thred pressure tube equipped with
bushing and plunger valve containing vinyl chloride (5 mL, 0.072
mol), solvent (dioxane, 10 mL), initiator (ethyl
2-bromoisobutyrate, 111 mg, 0.56 mmol), catalyst (samarium, 102 mg,
0.68 mmol) and ligand (bpy, 150 mg, 0.96 mmol) was degassed by
three freeze-vacuum pump-thaw cycles and filled with argon. The
reaction mixture was slowly heated to 90.degree. C. in an oil bath.
After 19 hours, the tube was slowly cooled and excess vinyl
chloride was allowed to boil off. Methylene chloride (10 mL) was
added and the solution was precipitated into methanol, filtered and
dried to yield 0.49 g (11%) of PVC, Mn=11,400, Mw/Mn=1.64.
Table 4, Example 144
A 50 mL Ace Glass 8648 #15 Ace-Thred pressure tube equipped with
bushing and plunger valve containing vinyl chloride (5 mL, 0.072
mol), solvent (o-DCB, 10 mL), initiator (ethyl 2-bromoisobutyrate,
111 mg, 0.56 mmol), catalyst (zinc, 45 mg, 0.69 mmol) and ligand
(bpy, 200 mg, 0.96 mmol) was degassed by three freeze-vacuum
pump-thaw cycles and filled with argon. The reaction mixture was
slowly heated to 90.degree. C. in an oil bath. After 20 hours, the
tube was slowly cooled and excess vinyl chloride was allowed to
boil off. Methylene chloride (10 mL) was added and the solution was
precipitated into methanol, filtered and dried to yield 0.49 g
(11%) of PVC, Mn=11,400, Mw/Mn=1.64.
Table 4, Example 145
A 50 mL Ace Glass 8648 #15 Ace-Thred pressure tube equipped with
bushing and plunger valve containing vinyl chloride (5 mL, 0.072
mol), solvent (o-DCB, 10 mL), initiator (1-chloro-cyanoethane, 111
mg, 0.56 mmol) and catalyst (chromium hexacarbonyl Cr(CO).sub.6,
150 mg, 0.68 mmol) was degassed by three freeze-vacuum pump-thaw
cycles and filled with argon. The reaction mixture was slowly
heated to 90.degree. C. in an oil bath. After 20 hours, the tube
was slowly cooled and excess vinyl chloride was allowed to boil
off. Methylene chloride (10 mL) was added and the solution was
precipitated into methanol, filtered and dried to yield 0.4 g (9%)
of PVC, Mn=18,400, Mw/Mn=1.57.
Table 6, Example 154
A 50 mL Ace Glass 8648 #15 Ace-Thred pressure tube equipped with
bushing and plunger valve containing vinyl chloride (5 mL, 0.072
mol), deionized water 10 mL), initiator (1-iodo-1-chloroethane, 137
mg, 0.72 mmol), catalyst (copper, 92 mg, 1.44 mmol), ligand (TREN,
421 mg, 2.88 mmol) and surfactant
(CH.sub.3--(CH.sub.2).sub.11--SO.sub.3Na, NaDDS, sodium
dodecylsulfate), 104 mg, 0.36 mmol) was degassed by three
freeze-vacuum pump-thaw cycles and filled with argon. The reaction
mixture was stirred at 20.degree. C. in an oil bath. After 20
hours, the tube was slowly opened and excess vinyl chloride was
allowed to boil off. THF (10 mL) was added and the mixture was
precipitated into methanol, filtered and dried to yield 4.3 g (95%)
of PVC, Mn=13,200, Mw/Mn=1.54.
Table 6, Example 218
A 50 mL Ace Glass 8648 #15 Ace-Thred pressure tube equipped with
bushing and plunger valve containing vinyl chloride (5 mL, 0.072
mol), deionized water 6 mL and THF 4 mL), initiator (iodoform, 284
mg, 0.72 mmol), catalyst (copper telluride, 367 mg, 1.44 mmol),
ligand (TREN, 421 mg, 2.88 mmol) and surfactant
(CH.sub.3--(CH.sub.2).sub.11--SO.sub.3Na, NaDDS, sodium
dodecylsulfate), 63 mg, 0.21 mmol) was degassed by three
freeze-vacuum pump-thaw cycles and filled with argon. The reaction
mixture was stirred at 20.degree. C. in an oil bath. After 14
hours, the tube was slowly opened and excess vinyl chloride was
allowed to boil off. THF (10 mL) was added and the mixture was
precipitated into methanol, filtered and dried to yield 4.5 g (99%)
of PVC, Mn=11,600, Mw/Mn=1.53.
Examples of Preparation of the Chlorine Containing Polymer
Utilizing a Non-Metallic Catalyst
Materials. Vinyl chloride (VC, 99%) was provided by OxyVinyls.
Iodoform (99%), and sodium dithionate (85%) were purchased from
Lancaster. Chloroform (99%), and bromoform (99%) were purchased
from ACROS Organics. Tetrahydrofuran (THF, 99%), methylene chloride
(99.5%), and methanol (99.8%) were purchased from Fisher
Scientific. Alcotex.RTM. 72.5 was purchased from Harlow Chemical
Co., UK. Methocel.RTM. F50 was purchased from the Dow Chemical
Company. All other chemicals were purchased from Aldrich and used
as received.
Techniques. .sup.1H- and .sup.13C-NMR spectra were recorded on a
Bruker DRX500 at 20.degree. C. in CDCl.sub.3 or CD.sub.2Cl.sub.2
with tetramethylsilane (TMS) as internal standard. GPC analysis was
performed on a Perkin-Elmer Series 10 high-pressure liquid
chromatograph equipped with an LC-100 column oven (22.degree. C.),
a Nelson Analytical 900 Series integrator data station, a
Perkin-Elmer 785A UV-Vis Detector (254 nm), a Varian Star 4090 RI
detector and 2 AM gel (10 .mu.m, 500 .ANG. and 10 .mu.m, 10.sup.4
.ANG.) columns. Number and weight-average molecular weights were
determined against polystyrene standards and were corrected using
the Universal Calibration with the following Mark-Houwink
parameters for PVC: K=1.50.times.10.sup.-2 mL/g, a=0.77.
The polymerizations reported were performed as follows unless
otherwise noted: a 50 mL Ace Glass 8648 #15 Ace-Thred pressure tube
equipped with bushing and plunger valve was charged with 9 ml of a
previously degassed appropriate mixture of water and THF then
filled with argon, closed and frozen using MeOH/dry ice. The
initiator (0.22 mmol), catalyst (0.43 mmol), buffer (4.8 mmol),
optional additive and precondensed VC (3 mL, 0.043 mol) were then
added. The exact amount of VC is determined gravimetrically after
the reaction. The tube was closed and degassed through the plunger
valve by applying reduced pressure and backfilling the tube with
Argon 15 times at -40.degree. C. The valve was closed and the
reaction mixture was stirred in a water bath at 25.degree.
C..+-.0.5.degree. C., behind a protective shield. After the
specified reaction time the tube was slowly opened. The excess of
VC was allowed to evaporate and the mixture was poured into MeOH
(150 mL). The polymer was ground mechanically, recovered by
filtration, then dried in a vacuum oven to a constant weight. The
conversion was determined gravimetrically. The kinetic plots were
constructed from individual experiments, as sampling of the
reaction is not possible.
The samples used for spectral analysis were precipitated twice from
THF or CH.sub.2Cl.sub.2 solutions in MeOH and dried under
vacuum.
A number of polymerization reactions were produced in accordance
with the above description. Selected examples from the Tables 1 8
are presented below.
Table 7, Example 14.
A 50 mL Ace Glass 8648 #15 Ace-Thred pressure tube equipped with
bushing and plunger valve was charged with a previously degassed
mixture of water (6 mL) and THF (3 mL), then filled with argon,
closed and frozen using MeOH/dry ice. Then, the initiator
(CHI.sub.3, 85.5 mg, 0.22 mmol), catalyst (Na.sub.2S.sub.2O.sub.4,
75.6 mg, 0.43 mmol), buffer (NaHCO.sub.3, 40.1 mg, 0.48 mmol), and
precondensed VC (3 mL, 0.043 mol) were added. The exact amount of
VC was determined gravimetrically after the reaction. The tube was
closed and degassed through the plunger valve by applying reduced
pressure and filling the tube with Ar 15 times at -40.degree. C.
The valve was closed and the reaction mixture was stirred in a
water bath at 25.degree. C..+-.0.5.degree. C., behind a protective
shield. After 33 h, the tube was slowly opened and the excess of VC
was allowed to evaporate and the mixture was poured into MeOH (150
mL). The polymer was ground mechanically, recovered by filtration
and dried in a vacuum oven to constant weight to give 1.78 g
(66.1%) PVC, M.sub.n=8,195; M.sub.w/M.sub.n=1.465.
Table 8, Example 44.
A 50 mL Ace Glass 8648 #15 Ace-Thred pressure tube equipped with
bushing and plunger valve was charged with Brij.RTM. 98 (6.3 mg 5.5
.mu.mol), a previously degassed mixture of water and THF (volume
ratio 7/3, 9 mL), then filled with argon, closed and frozen using
MeOH/dry ice. The initiator (CHI.sub.3, 85.5 mg, 0.22 mmol),
catalyst (Na.sub.2S.sub.2O.sub.4, 75.6 mg, 0.43 mmol), buffer
(NaHCO.sub.3, 40.1 mg, 0.48 mmol), and precondensed VC (3 mL, 0.043
mol) were then added. The exact amount of VC is determined
gravimetrically after the reaction. The tube was closed and
degassed through the plunger valve by applying reduced pressure and
filling the tube with Ar 15 times at -40.degree. C. The valve was
closed and the reaction mixture was stirred in a water bath at
25.degree. C..+-.0.5.degree. C. behind a protective shield. After
44 h, the tube was slowly opened and the excess of VC was allowed
to evaporate and the mixture was poured into MeOH (150 mL). The
polymer was ground mechanically, recovered by filtration and dried
in a vacuum oven to constant weight to give 2.16 g (72.18%) PVC,
M.sub.n=9,325; M.sub.w/M.sub.n=1.487.
Table 9, Example 73.
A 50 mL Ace Glass 8648 #15 Ace-Thred pressure tube equipped with
bushing and plunger valve was charged with Brij.RTM. 98 (6.3 mg 5.5
.mu.mol), a previously degassed mixture of water and THF (volume
ratio 7/3, 9 mL), then filled with argon, closed and frozen using
MeOH/dry ice. The initiator (CHI.sub.3, 85.5 mg, 0.22 mmol),
catalyst (Na.sub.2S.sub.2O.sub.4, 75.6 mg, 0.43 mmol), buffer
(NaHCO.sub.3, 40.1 mg, 0.48 mmol), optional electron shuttle
(OV.sup.2+, 0.2 mg, 0.39 .mu.mol), and precondensed VC (3 mL, 0.043
mol) were then added. The exact amount of VC was determined
gravimetrically after the reaction. The tube was closed and
degassed through the plunger valve by applying reduced pressure and
filling the tube with Ar 15 times at -40.degree. C. The valve was
closed and the reaction mixture was stirred in a water bath at
25.degree. C..+-.0.5.degree. C. behind a protective shield. After
66 h, the tube was slowly opened and the excess of VC was allowed
to evaporate and the mixture was poured into MeOH (150 mL). The
polymer was ground mechanically, recovered by filtration and dried
in a vacuum oven to constant weight to give 2.50 g (83.22%) PVC,
M.sub.n=10,455; M.sub.w/M.sub.n=1.592.
Table 10, Example 100.
A 50 mL Ace Glass 8648 #15 Ace-Thred pressure tube equipped with
bushing and plunger valve was charged with Brij.RTM. 98 (6,3 mg 5.5
.mu.mol), a previously degassed mixture of water and THF (volume
ratio 2/1, 9 mL), then filled with argon, closed and frozen using
MeOH/dry ice. The initiator (CHI.sub.3, 85.5 mg, 0.22 mmol),
catalyst (Na.sub.2S.sub.2O.sub.4, 75.6 mg, 0.43 mmol), buffer
(NaHCO.sub.3, 40.1 mg, 0.48 mmol), optional electron shuttle
(MV.sup.2+, 0.1 mg, 0.39 .mu.mol), and precondensed VC (3 mL, 0.043
mol) were then added. The exact amount of VC was determined
gravimetrically after the reaction. The tube was closed and
degassed through the plunger valve by applying reduced pressure and
filling the tube with Ar 15 times at -40.degree. C. The valve was
closed and the reaction mixture was stirred in a water bath at
25.degree. C..+-.0.5.degree. C. behind a protective shield. After
24 h, the tube was slowly opened and the excess of VC was allowed
to evaporate and the mixture was poured into MeOH (150 mL). The
polymer was ground mechanically, recovered by filtration and dried
in a vacuum oven to constant weight to give 2.28 g (75.90%) PVC,
M.sub.n=10,174; M.sub.w/M.sub.n=1.516.
Table 11, Example 106.
A 50 mL Ace Glass 8648 #15 Ace-Thred pressure tube equipped with
bushing and plunger valve was charged with a previously degassed
mixture of water (6 mL) and THF (3 mL), then filled with argon,
closed and frozen using MeOH/dry ice. The initiator (CHBr.sub.3,
26.2 mg, 0.22 mmol), catalyst (Na.sub.2S.sub.2O.sub.8, 102.4 mg,
0.43 mmol and HCOONa, 29.2 mg, 0.43 mmol), buffer (NaHCO.sub.3,
40.1 mg, 0.48 mmol), and precondensed VC (3 mL, 0.043 mol) were
then added. The exact amount of VC was determined gravimetrically
after the reaction. The tube was closed and degassed through the
plunger valve by applying reduced pressure and filling the tube
with Ar 15 times at -40.degree. C. The valve was closed and the
reaction mixture was stirred in a water bath at 25.degree.
C..+-.0.5.degree. C. behind a protective shield. After 120 h, the
tube was slowly opened and the excess of VC was allowed to
evaporate and the mixture was poured into MeOH (150 mL). The
polymer was ground mechanically, recovered by filtration and dried
in a vacuum oven to constant weight to give 1.61 g (53.74%) PVC,
M.sub.n=8,593; M.sub.w/M.sub.n=1.968.
Table 12, Example 110.
A 50 mL Ace Glass 8648 #15 Ace-Thred pressure tube equipped with
bushing and plunger valve was charged with a previously degassed
mixture of water (6 mL) and THF (3 mL), then filled with argon,
closed and frozen using MeOH/dry ice. The initiator (CHCl.sub.3,
26.2 mg, 0.22 mmol), catalyst (Na.sub.2S.sub.2O.sub.8, 102.4 mg,
0.43 mmol and HCOONa, 29.2 mg, 0.43 mmol), buffer (NaHCO.sub.3,
40.1 mg, 0.48 mmol), and precondensed VC (3 mL, 0.043 mol) were
then added. The exact amount of VC was determined gravimetrically
after the reaction. The tube was closed and degassed through the
plunger valve by applying reduced pressure and filling the tube
with Ar 15 times at -40.degree. C. The valve was closed and the
reaction mixture was stirred in a water bath at 25.degree.
C..+-.0.5.degree. C. behind a protective shield. After 96 h, the
tube was slowly opened, the excess of VC was allowed to evaporate
and the mixture was poured into MeOH (150 mL). The polymer was
ground mechanically, recovered by filtration and dried in a vacuum
oven to constant weight to give 1.78 g (58.15%) PVC, M.sub.n=8,854;
M.sub.w/M.sub.n=2.154.
Table 13, Example 116
A 50 mL Ace Glass 8648 #15 Ace-Thred pressure tube equipped with
bushing and plunger valve was charged with a previously degassed
mixture of water and THF (volume ratio 7/3, 9 mL), then filled with
argon, closed and frozen using MeOH/dry ice. The initiator
(CHI.sub.3, 85.5 mg, 0.22 mmol), catalyst
(H.sub.2NC(.dbd.NH)SO.sub.2H, 46.9 mg, 0.43 mmol), buffer
(NaHCO.sub.3, 80.2 mg, 0.95 mmol), optional electron shuttle
(OV.sup.2+, 0.2 mg, 0.39 .mu.mol), and precondensed VC (3 mL, 0.043
mol) were then added. The exact amount of VC was determined
gravimetrically after the reaction. The tube was closed and
degassed through the plunger valve by applying reduced pressure and
filling the tube with Ar 15 times at -40.degree. C. The valve was
closed and the reaction mixture was stirred in a water bath at
25.degree. C..+-.0.5.degree. C. behind a protective shield. After
68 h, the tube was slowly opened and the excess of VC was allowed
to evaporate and the mixture was poured into MeOH (150 mL). The
polymer was ground mechanically, recovered by filtration and dried
in a vacuum oven to constant weight to give 1.65 g (69.87%) PVC,
M.sub.n=7,119; M.sub.w/M.sub.n=1.489.
Table 14, Example 126.
A 50 mL Ace Glass 8648 #15 Ace-Thred pressure tube equipped with
bushing and plunger valve was charged with a previously degassed
mixture of water and THF (volume ratio 7/3, 9 mL), then filled with
argon, closed and frozen using MeOH/dry ice. The initiator
(CHI.sub.3, 85.5 mg, 0.22 mmol), catalyst (Na.sub.2S.sub.2O.sub.4,
75.6 mg, 0.43 mmol), buffer (NaHCO.sub.3, 40.1 mg, 0.48 mmol),
optional electron shuttle (OV.sup.2+, 0.2 mg, 0.39 .mu.mol) and
optional additive (Nal, 263 mg, 1.76 mmol), and precondensed VC (3
mL, 0.043 mol) were then added. The exact amount of VC was
determined gravimetrically after the reaction. The tube was closed
and degassed through the plunger valve by applying reduced pressure
and filling the tube with Ar 15 times at -40.degree. C. The valve
was closed and the reaction mixture was stirred in a water bath at
25.degree. C..+-.0.5.degree. C. behind a protective shield. After
66 h, the tube was slowly opened and the excess of VC was allowed
to evaporate and the mixture was poured irito MeOH (150 mL). The
polymer was ground mechanically, recovered by filtration and dried
in a vacuum oven to constant weight to give 2.10 g (69.87%) PVC,
M.sub.n=8,915; M.sub.w/M.sub.n=1.445.
* * * * *